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A cytotoxic ruthenium tris(bipyridyl) complex that accumulates at plasma membranes.
technische universität
dortmund
2023
SCIENTIFIC HIGHLIGHTS
Annual Report
Fakultät Bio- und
Chemieingenieurwesen
SCIENTIFIC HIGHLIGHTS 2023
Page 2
Content
Department of BCI
Preface
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Equipment Design (AD)
Extending Ontologies Assisted by Natural Language Processing
Artificial Intelligence-assisted engineering for process technology
AI-assisted sensing and modular control for process equipment and plants
Two-Phase Flow Reaction System for DNA-Encoded Amide Coupling
Reaction engineering tools for flow process engineering
Spatially and Temporally Resolved 3D-Analysis of Bubble Formation in Capillary Flows
Smart Image Sensor for Liquid-liquid Systems
Quasi-Continuous Production of Solids in a Modular and Small-Scale Plant
Numerical modelling of the discharge behavior of particles from gas vessel
Real-World Szenario in a Laboratory Experiment on a Digital Twin to foster Work 4.0 Skills
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Publications
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Plant and Process Design (APT)
Modeling of Continuous Slug Flow Cooling Crystallization towards Pharmaceutical Application
End-to-End Continuous Small-Scale Drug Substance Manufacturing: From Continuous in-situ Nucleator to Free
Flowing Crystalline Particles
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Publications
25
Biomaterials and Polymer Science (BMP)
Catching and Releasing of Antibiotic Worm Micelles
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Publications
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Bioprocess Engineering (BPT)
Bivariate One Strain Many Compounds Designs Expand the Secondary Metabolite Production Space in
Corallococcus coralloides
Reaction Engineering and Comparison of Electroenzymatic and Enzymatic ATP Regeneration Systems
32
Publications
35
Computational Bioengineering (CBE)
Tailoring Chemical Reactivity on Metal Surfaces
Towards therapeutic alternatives targeting the chemokine receptor CXCR4
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40
Publications
41
Computational Systems Biology (CSB)
The pseudoentropy of allele frequency trajectories, the persistence of variation, and the effective population size
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45
Publications
46
Solids Process Engineering (FSV)
UV/Vis spectroscopy as a real-time release tool for pharmaceutical tablets
Predicting Key Process Parameters in Pharmaceutical Hot Melt Extrusion
Increased Drug Dissolution by Embedding of Micro-Particles
Evolutionary Optimization of Filter Media
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Publications
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SCIENTIFIC HIGHLIGHTS 2023
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Fluid Separations (FVT)
Recent Developments in Rotating Packed Bed Technology
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Publications
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Process Automation Systems (PAS)
60
Improving the control performance of a model predictive controller with reinforcement learning for chemical processes 61
Sobolev Training for Data-efficient Approximate Nonlinear MPC
62
Publications
63
Reaction Engineering and Catalysis (REC)
Flow characterization of additively manufacturable periodic open cellular structures in the context
of heterogeneous catalysis
Dynamically Operated Fixed Bed Reactors for CO2 Methanation
Process Intensification of Gas-Liquid Reactors
66
Publications
70
Technical Biochemistry (TB)
Improving CBCA synthase activity through rational protein design
Generation of Cannabigerolic Acid Derivatives and Their Precursors by Using the Promiscuity of the Aromatic
Prenyltransferase NphB
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Publications
75
Technical Biology (TBL)
New Antiparasitic Drugs by Whole-Cell Biotransformation
Biocatalytic Flow Synthesis of Heterocycles
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78
Publications
79
Industrial Chemistry (TC)
Polymer-Grade Bio-Monomers from Oleochemicals by Combining Homogeneous Catalysis and Selective Product
Crystallization in an Integrated Process
Development of Eco-Friendly and Sustainable PET Glycolysis Using Sodium Alkoxides as Catalyst
Stable and Continuous Production of Amines via Reductive Amination in a Green Switchable Solvent System
with Efficient Water Removal
Continuous production of amines directly from alkenes via cyclodextrin-mediated hydroaminomethylation
using only water as the solvent
80
Publications
85
Thermodynamics (TH)
Continuous Non-Centrifugal Phase Separation in Biphasic Whole-Cell Biocatalysis
Effects of solvent and of catalyst on the acid-catalyzed esterification of levulinic acid via activity-based models
Modeling the impact of tablet surface layers on the dissolution rate in water
Carboxylation of Acetylene without Salt Waste: Using thermodynamic predictions to optimize the catalyst
and the reaction solvent
Direct Generation of Compressed Air from Waste Heat by Cascaded Thermocompressors with SelfExcited Overdriven Free Displacers
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Publications
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Transport Processes (TP)
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Publications
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SCIENTIFIC HIGHLIGHTS 2023
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Hannsjörg Freund
Toni Goßmann
Christoph Held
Oliver Kayser
Norbert Kockmann
Sergio Lucia
Stephan Lütz
Markus Nett
Gabriele Sadowski
Elsa Sánchez García
Gerhard Schembecker
Markus Thommes
Jörg C. Tiller
Dieter Vogt
Alba Diéguez Alonso
Department of BCI
SCIENTIFIC HIGHLIGHTS 2023
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Preface
Dear Reader,
Annually publishing the „Best of Science” of the Department of Bio- and Chemical Engineering of the TU Dortmund has
become a long-standing tradition. The present Scientific Highlights of the year 2023 – the 14th edition - are testament
of the booming research activities of the department. They include many aspects of modern process engineering in the
chemical, biochemical, and pharmaceutical industry. Focus of the Highlights are often sustainability and computational
science. The scientific work was mostly achieved by our students in their bachelor, masters, and doctoral theses, which
are the backbone of our department. The faculty is composed of engineers, chemists, pharmacists, and computer scientists. This ensemble was strengthened last year by Prof. Alba Diéguez Alonso, who is leading the group of transport
processes. She is working on biomass conversion, which as greatly adding to our main research emphasis sustainability.
I wish her a great start. I hope the present collection of Scientific Highlights inspires you, the readers, to remain or become our collaboration partners.
Enjoy the reading,
Prof. Joerg C. Tiller
SCIENTIFIC HIGHLIGHTS 2023
Equipment Design (AD)
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SCIENTIFIC HIGHLIGHTS 2023
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Extending Ontologies Assisted by Natural Language Processing
Gathering the semantic knowledge for FAIR data management by automated text crawling
Alexander S. Behr, Lukáš Korel, Uladzislau Yorsh, Martin Holeňa, Norbert Kockmann
Ontologies store semantic knowledge in a machine-readable way and represent domain knowledge in controlled and
connected vocabulary. Human-readable texts often contain a lot of semantic knowledge. With natural language processing
(NLP) methods, it is possible to extend ontologies with text-based semantic information, facilitating Findable, Accessible,
Interoperable, Reusable (FAIR) data workflows. In order to compare different ontologies, the textual definitions of the
vocabulary are contrasted using NLP.
Ontologies facilitate the formalized expression of knowledge, providing explicit representation of knowledge. As
manual creation leads to diverse representations, ways
to extend and develop ontologies using natural language
processing (NLP) techniques were investigated.
First, automating the selection of relevant ontologies for
scientific texts to reduce experts' workload was studied.
The overall workflow is depicted in Figure 1 and could be
used to classify scientific texts. With this, the ontologies
fitting best to the text can be determined, leading to automated labeling of textual data, fit for further use in machine learning applications. Significant differences between scientific texts and ontology annotations were
identified, prompting a proposal for an entity recognition
step utilizing various classifiers. Testing this in fields related to the domain of catalysis research, the Support Vector
Machine displayed the highest confidence and margin.
With no ground truth for article classification, methods to
mitigate the impact were investigated, including interpolation between annotations using public alternatives to
GPT. Future experiments aim to explore various transformers, leverage neural networks, and extend ontologies
using graph neural networks. [1]
In another study, the automatic extension of ontologies
using NLP techniques was demonstrated, focusing on a
text dataset related to catalytic methanation of CO2. The
workflow also depicted in Figure 2 involves extracting
concepts from the text, annotating them using NLP, and
extending ontologies with new classes and relations. In a
proof-of-concept with 28 papers, the workflow annotates
68.97% of text-based concepts and automatically enriches the Allotrope Foundation Ontology with 90 new classes,
74.44% of which are annotated.
With a graph-based approach, a preliminary safety analysis was developed for early integration into automated engineering workflows [3], see Figure 2.
Figure 2: Workflow of code to extend an ontology by new classes based on text
dataset. The ontology used as input is denoted red, while the extended ontology,
which poses the output of the workflow is colored green. [2, 3]
The adaptable workflow can be applied to other ontologies and text datasets, facilitating automated ontology
development for research data annotation in domains like
catalysis and process engineering. However, further evaluation by domain experts is recommended to assess the
workflow's usefulness in automatically generating valuable classes and relations [2,3].
Figure 1: Overall workflow for text-to-ontology mapping via NLP with to search for
relevant ontologies in catalysis research leading to classified text paragraphs fit
for further application in e.g. machine learning. [1]
Contact:
norbert.kockmann@tu-dortmund.de
Publications:
[1] L. Korel, U. Yorsh, A. S. Behr, N. Kockmann, M. Holeňa, Textto-Ontology Mapping via Natural Language Processing with
Application to Search for Relevant Ontologies in Catalysis, MDPIcomputers, 12, 14, 2023, doi.org/10.3390/computers12010014
[2] A. S. Behr, M. Völkenrath, N. Kockmann, Ontology extension
with NLP-based concept extraction for domain experts in
catalytic sciences, Knowledge and Information Systems, 65(12),
5503–5522, 2023, doi.org/10.21203/rs.3.rs-3491129/v1
[3] A. S. Behr, M. Völkenrath, M. Ben Moussa, N. Kockmann,
Natural Language Processing-Based Term Extraction for
Concept Enrichment of Ontologies for Catalysis Research, 56.
Jahrestagung Deutscher Katalytiker, Weimar, 15.-17.03.2023
SCIENTIFIC HIGHLIGHTS 2023
Page 8
Artificial Intelligence-assisted engineering for process technology
AI methods exhibit a large potential in assisting the engineering activities in process industries.
Jonas E. Oeing, Laura M. Neuendorf, Norbert Kockmann
Smart process engineering is a thriving topic in the frame of AI tool development. From AI-supported supervision in
stirred extraction columns to preliminary safety analysis, and leveraging graph learning of plant topology data, the tools
for improved efficiency and safety are developing. Automated P&ID evaluation, powered by DEXPI information, enables
streamlined and assisted workflows leading to enhanced productivity. The roadmap ahead is defined by tool´s integration,
marking a paradigm shift towards smarter engineering workflows.
The current rapid development of AI-supported methods
also affects the process industry and related research.
The Laboratory of Equipment Design was co-initiator of
the KEEN project (www.keen-plattform.de) and co-edited
a special issue of the project´s results in the journal Chemie-Ingenieur-Technik [1]. Beside smart sensor technology
[2], the engineering workflow from conceptual design over
safety considerations in the early engineering phase [3] to
automated processing of pipe & instrumentation diagrams
in DEXPI format [4, 5] were addressed (Figure 1) and exhibit new opportunities for engineering activities.
A basic requirement for AI tools in process engineering
activities is the graph learning in machine-readable plant
topology data, here the DEXPI format as well-established,
but still developing standard. This assists the necessary
shift from a document-oriented to a data-oriented process industry, in particular for describing piping and instrumentation diagrams (P&ID). In the contribution on graph
learning [4], industry, software vendors, and research institutions have joined forces to demonstrate the current
developments and potentials of machine-readable P&IDs
in the DEXPI format combined with artificial intelligence.
The aim is to use graph neural networks to learn patterns
in machine-readable P&ID data, which results in the efficient engineering and development of new P&IDs. The tool
enables for example real-time detection of inconsistencies (e.g. missing equipment or faulty connections). This
reduces the development time in detail engineering due
to a decrease in error rate and a resulting time saving.
With a graph-based approach, a preliminary safety analysis was developed for early integration into automated engineering workflows [3], see Figure 2.
Figure 1: Web-based topology display of a storage vessel in an IIoT platform.
Here: a DEXPI plant topology in PTC ThingWorx
Publications:
[1] M. Bortz, K. Dadhe, S. Engell, V. Gepert, N. Kockmann, R. MüllerPfefferkorn, T. Schindler, L. Urbas, AI in Process Industries – Current
Status and Future Prospects, Chem. Ing. Technik, 95(7), 975-988,
2023, doi.org/10.1002/cite.202200247
[2] L. Neuendorf, Z. Hammal, A. Fricke, N. Kockmann, AI-based
supervision for a stirred extraction column assisted with
population balance-based simulation, Chem. Ing. Technik, 95(7),
1134-1145, 2023, doi.org/10.1002/cite.202200241
[3] J. Oeing, T. Holtermann, W. Welscher, N. Kockmann, preHAZOP:
Graph-based safety analysis for early integration into automated
engineering workflows, Chem. Ing. Technik, 95(7), 1083-1095, 2023,
doi.org/10.1002/cite.202200222
[4] J. Oeing, K. Brandt, M. Wiedau, G. Tolksdorf, W. Welscher, N.
Kockmann, Graph Learning in Machine-Readable Plant Topology
Data, Chem. Ing. Technik, 95(7), 1049-1060, 2023, doi.org/10.1002/
cite.202200223
[5] A. Klose, D. Wagner-Stürz, L. Neuendorf, J. Oeing, V. Khaydarov,
M. Schleehahn, N. Kockmann, L. Urbas, Automated Evaluation of
Biochemical Plant KPIs based on DEXPI Information, Chem. Ing.
Technik, 95(7), 1165-1171, 2023, doi.org/10.1002/cite.202200239
Figure 2: Approach for automated safety analyses with graph-based plant &
process models using a deterministic preHAZOP algorithm.
The combination of DEXPI information with those from
process simulation enables evaluation of safety-critical
scenarios can be in an initial risk assessment.
Contact:
norbert.kockmann@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 9
AI-assisted sensing and modular control for process equipment and plants
Smart equipment needs new sensors and control measures for improved operations.
Lukas Bittorf, Laura M. Neuendorf, Jonas E. Oeing, Piriyanth Sakthithasan, Norbert Kockmann
For transforming the process industry, AI-driven smart sensors aligned with modular automation standards enhance
efficiency in process development and operation. Tailored modular automation with modular type package MTP services
are necessary for modular units and process analytics for higher efficiency and robustness. These novel measures are
used for advanced extraction cells for improved process conditions. Crystal detection and characterization are supported
by convolutional neural networks CNNs for precise size distribution analysis.
Embracing AI for heightened performance and accuracy
doesn´t means only new computer algorithms, but also
generating a better data base for these tools. Modular automation with design of MTP services for different downstream units and process analytic technology following
VDI/VDE/NAMUR 2658 standards [1]. The combination of
modular equipment with own automation capability together with an overarching orchestration layer, flexible
and rapid adaptation of the plant is possible for new processes, e.g. the distillation of high boiling organic acids [2],
see Figure 1.
vent extraction column, a glass-metal stirred cell was
modularly designed for higher temperature and pressure,
see Figure 2. Increased temperature range improved the
mass transfer, too, and led to improved separation performance with higher mass throughput [5].
Figure 2: Modular setup of laboratory DN 15 solvent extraction
column with periphery units [5].
Contact:
norbert.kockmann@tu-dortmund.de
Figure 1: Modular setup of laboratory DN 25 spinning band distillation column
and periphery units [1].
In a further step, a digital camera was developed as Artificial Intelligence-based MTP-compatible smart sensor
for improved process sensing, control, and automation.
Beside a liquid-liquid extraction column, a fermenter was
equipped with the digital camera to observe the flooding
conditions during aeration of the fermentation broth [3].
Computer vision, powered by convolutional neural networks (CNNs), has been applied to processes like continuous cooling crystallization [4]. Crystals formed in a draft
tube baffle crystallizer were monitored in real-time with
particle size distribution for optimizing crystal growth and
product quality. To widen the operational range of the sol-
Publications:
[1] L. Bittorf, J. Oeing, T. Kock, R. Garreis, N. Kockmann, Design of
MTP services for modular downstream units and process analytic
technology, Chem. Eng. & Technol., 46(7), 1502-1510, 2023, doi.
org/10.1002/ceat.202200390
[2] V. Elhami, L.M. Neuendorf, T. Kock, N. Kockmann, B. Schuur,
Separation of Crotonic Acid and 2-Pentenoic Acid Obtained by
Pyrolysis of Bio-Based Polyhydroxyalkanoates Using a Spinning
Band Distillation Column, ACS Sustain. Chem. Eng., 11(12), 46994706, 2023, doi.org/10.1021/acssuschemeng.2c07046
[3] L. Neuendorf, V. Khaydarov, C. Schlander, T. Kock, J. Fischer. L.
Urbas, N. Kockmann, Artificial Intelligence-based Module Type
Package (MTP)-compatible Smart Sensors in the Process Industry,
Chem. Ing. Technik, 95(10), 1546-1554, 2023, doi.org/10.3389/
fchem.2023.1244043
[4] L. Neuendorf, S. Höving, L. Bennemann, N. Kockmann, Detecting
crystals in suspensions: convolutional neural networks vs. a gravity
based approach for size distribution detection, Chem. Ing. Technik,
95(7), 1146-1153, 2023, doi.org/10.1002/cite.202200235
[5] P. Sakthithasan, L. Orth, M. Venhuis, N. Kockmann, Design
of a process intensified liquid-liquid extraction cell for higher
temperature and pressure, Chem. Eng. & Technol., 46(5), 882-890,
2023, doi.org/10.1002/ceat.202200550
SCIENTIFIC HIGHLIGHTS 2023
Page 10
Two-Phase Flow Reaction System for DNA-Encoded Amide Coupling
More process information for efficient and reliable process control
Robin Dinter, Suzanne Willems, Mahdi Hachem, Yana Streltsova, Andreas Brunschweiger, Norbert Kockmann
DNA‑encoded library (DEL) technologies benefit from automated flow chemistry platforms to facilitate reaction
development, building block validation, and high‑throughput library synthesis. A liquid-liquid two-phase flow reactor
system was designed to enable parallel conduction of reactions with DNA‑labeled substrates. The dispersed phase (DP) in
the capillary slug flow contained the DNA reaction mixtures, including various carboxylic acids (CA). Fluorocarbon oil FC 40
was introduced as an inert continuous phase (CP) to prevent backmixing. The slugs were successfully generated to act as
individual reaction compartments, representing single batch experiments and enabling parallelized reactions. As a widely
used exemplar DEL reaction, the amide coupling reaction was successfully transferred from batch to flow chemistry and
DNA integrity was ensured.
For process intensification, the coiled flow inverter (CFI)
concept was adapted to the DNA encoded chemistry requirements, which considers µL scale reactions, DNA integrity throughout the process, and recovery of the product fraction from the excess unreacted starting material.
The tailored CFI for DNA labeled substrates was applied to
a liquid-liquid two phase setup, as shown in Figure 1. In order to obtain the µL scale reaction volume, a reproducible
slug flow regime was generated. The slugs were pumped
back and forth to achieve similar reaction times as in the
batch experiments.
flow reactor design was demonstrated by profiling the reactivity of a small scope of diverse substituted CA, as
shown in Figure 2. The main objective in the production of
a DEL with different building blocks is to avoid cross contamination. All amide coupling reactions were run in one
flow setup for 8 h, with each individual reaction divided
into 7 µL slugs. Only the expected product peaks were observed in the MALDI-MS spectra, and no products from
other CAs were detected, ruling out cross contamination
between slugs containing two different CA. This underlines that the simultaneous reactions in the flow setup
worked successfully. In parallel, a batch reaction was performed to compare the performance of the flow.
Figure 1: Reaction setup to conduct the DNA encoded amide coupling reaction.
The DP was injected using a 250 µL syringe, and the CP using a 10 mL syringe.
Slugs were generated with a T junction and collected in microliter tubes for
analysis.
Next, the amide coupling reaction with DNA labeled substrates was effectively optimized and conducted in a flow
reaction system for the first time. The robustness of the
Publications:
[1] R. Dinter, S. Willems, M. Hachem, Y. Streltsova, A. Brunschweiger,
N. Kockmann, Development of a Two Phase Flow Reaction System
for DNA Encoded Amide Coupling, React. Chem. & Eng., 8, 1334–
1340, 2023, doi.org/10.1039/d3re00020f
[2] R. Dinter, S. Willems, T. Nissalk, O. Hastuerk, A. Brunschweiger,
N. Kockmann, Development of a Microfluidic Photochemical Flow
Reactor Concept by Rapid Prototyping, Front. Chem., 11, 1244043,
2023, doi.org/10.3389/fchem.2023.1244043
[3] R. Dinter, K. Götte, F. Gronke, L. Justen, A. Brunschweiger,
N. Kockmann, Development of an Automated Flow Chemistry
Affinity‑Based Purification Process for DNA‑Encoded Chemistry, J.
Flow Chem., 13, 361–373, 2023, doi.org/10.1007/s41981-023-00282-0
Figure 2: Profiling results of various carboxylic acids (CA) 3 conducted in batch and
the flow reaction system after 8 h. A volumetric flow rate of 1.6 mL min-1 was set for
the flow experiments. The concentration of DNA-labeled amine 1 was 3.6 µmol L-1.
This study showed that the flow and batch setup gave
comparable results with moderate to full conversions for
a diverse set of CA. More importantly, FC-40 prevented
backmixing of the individual slugs without affecting the
amide coupling reaction. These results are a successful
step towards automatable DEL reactions.
Contacts:
robin.dinter@tu-dortmund.de
norbert.kockmann@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 11
Reaction engineering tools for flow process engineering
Flow chemistry doesn´t belong to the newest methods in reaction engineering, but still has room for
improvement.
Lisa Schulz, Waldemar Krieger, T. Aljoscha Frede, Norbert Kockmann
Flow chemistry is already an established tool in reaction engineering, however, adequate sensing and data analysis are
still under development. Reactive intermediates are investigated in the selective monosubstitution on trichlorosilane with
ultra-reactive organolithium compounds. With multivariate curve resolution, we facilitate kinetic modeling and scale-up
prediction. Seebeck elements in a microcalorimeter enable swift characterization of exothermic reactions supported by
data management with a modular Open-Source IoT Platform.
Reaction engineering belongs to the core of chemical
engineering and has already many tools in the box. Flow
chemistry is a still growing field. We investigated together with the CCB faculty the selective monosubstitution on
a trichlorosilane with highly reactive organolithium compounds in a microflow reactor [1]. Since there has been a
lack of use in substitution reactions, we used flow microreactors to controllably synthesize highly reactive organolithium compounds and thus create new synthetic opportunities.
Utilizing a microscale flow calorimeter, highly exothermic
reactions like thiosulfate oxidation were characterized
combined with reactor performance estimation [2].
Through the combination of CFD simulations with reactor
performance estimation, we achieved accurate conversion and temperature profiles within the microscale setup
(Figure 1). Our approach, tested rigorously for highly oxidative reactions of sodium thiosulfate, demonstrates excellent agreement between estimated and experimental
data, showcasing the reliability of our methodology.
Figure 1: Predicted temperature profile along the reaction channel for thiosulfate
oxidation.
For improved kinetic modeling and scale-up prediction, an
imine synthesis was investigated in an oscillating segmented flow microreactor at different temperatures using
non-invasive Raman spectroscopy [3]. Multivariate curve
resolution provided a calibration-free approach for obtaining the kinetic parameters. Taking heat and mass balance
into account, the proposed kinetic model was applied for a
model-based scale-up prediction from capillary flow
Contacts:
norbert.kockmann@tu-dortmund.de
onditions to a 0.5 L semi-batch reactor. Observed by inc
line Raman spectroscopy and off-line gas chromatography
analysis, the scale-up was successfully demonstrated
with good agreement between measured and predicted
concentration profiles (Figure 2).
Figure 2: Conversion and yield from multivariate modeling for imine synthesis from
benzaldehyde and benzylamine.
The microscale flow calorimeter was connected to the
modular open-source IoT-platform d-scover@ from d-fine
[4]. The existing OPC UA server was used to stream data
into the platform allowing for data visualization, storage,
and analysis. The low entry hurdle for operators with little to no programming experience is a key point, since all
essential tools for a researcher in the laboratory to store,
visualize, and evaluate the measured values are provided
without having to install them yourself. In addition, the use
of open-source program allows a quick exchange of programs between researchers and the community or forums
for help with issues.
Publications:
[1] M. Achternbosch, L. Zibula, A. Schmidt, W. Krieger, N. Kockmann, C.
Strohmann, Selective monosubstitution on a trichlorosilane with highly
reactive organolithium compounds in a microflow reactor, J. Flow Chem., 13,
9-12, 2023, doi.org/10.1007/s41981-022-00251-z
[2] T.A. Frede, N. Nikbin, N. Kockmann, Reactor Performance Estimation
in Microscale Flow Calorimeter for Rapid Characterization of Exothermic
Reactions, J. Flow Chem., 13, 31-44, 2023, doi.org/10.1007/s41981-022-00251-z
[3] L. Schulz, P. Stähle, S. Reining, M. Sawall, N. Kockmann, T. Röder,
Multivariate curve resolution for kinetic modeling and scale-up prediction, J.
Flow Chem., 13, 13-19. 2023, doi.org/10.1007/s41981-022-00252-y
[4] T.A. Frede, C. Weber, T. Christ, T. Brockhoff, D. Ludwig, N. Kockmann,
Data Management of a Microcalorimeter Using a Modular Open-Source IoT
Platform, MDPI-processes, 11(1), 2023, doi.org/10.3390/pr11010279
SCIENTIFIC HIGHLIGHTS 2023
Page 12
Spatially and Temporally Resolved 3D-Analysis of Bubble Formation in Capillary
Flows
Bastian Oldach, Max Schlickewei, Philipp Wintermeyer, Norbert Kockmann
Since its first report, microfluidics is an ever growing trend in various scientific fields and applications as it enables for
fast and efficient processes. A deep physical understanding of transport phenomena is essential for the precise control
of bubble-based microfluidics. Micro-computed tomography (μCT) is well suited as a non-invasive visualization tool, as
it enables for three-dimensional insights into multiphase flow patterns with high spatial resolution, but without need for
optical access. This contribution presents the first 3D analysis of bubble formation recorded using µCT.
The 3D analysis (image acquisition: Bruker Skyscan
1275 μCT scanner) provides new insights into bubble formation in different capillary geometries in the micron
range (image resolution ~ 15 µm). Image analysis based on
artificial intelligence methods is used to identify a defined
state of the dispersed phase for each angular position to
obtain 3D datasets of periodic flow phenomena. A schematic of the implemented setup inside the µCT and the
image evaluation routine can be seen in Figure 1. The investigations cover detailed insights into the squeezing and
leaking regimes during bubble formation in capillaries with
circular and rectangular cross section (dh = 1.6 mm). The
capillaries are manufactured using stereo lithography and
a clear resin.
The bubble volume, the maximum diameter, the interfacial
area, and the length of the detaching bubbles are decreasing as the bubble approaches the pinch off stage, as shown
in Figure 2. This effect is more relevant for channels of circular cross-sections, where the bubbles fill almost the entire capillary since corner flows prevent these phenomena
in rectangular capillaries. The data also provides information regarding the liquid wall film thickness, which approaches a constant value before the bubbles pinch off at
t* = 0.4. The phenomena are investigated with air as dispersed phase and polydimethylsiloxane as the continuous
phase for flow rates < 1 mL min-1.
Publications:
[1] B. Oldach, M. Schlickewei, P. Wintermeyer, N. Kockmann, µTAS
Conf. on Miniaturized Systems for Chemistry and Life Sciences,
Katowice, Poland, 15.-19.10.2023
[2] B. Oldach, C. Müller, P. Wintermeyer, N. Kockmann, 3D
investigation of droplet generation and coalescence in capillary
liquid-liquid flows using µ-computed tomography, µFIP Conf. Micro
Flow and Interfacial Phenomena, Evanston, IL, USA, 18.-21.6.2023
[3] B. Oldach, L. Ben Achour, C. Müller, P. Wintermeyer, N. Kockmann,
Continuous Liquid-Liquid Separation of Segmented Capillary
Flows, Flow Chemistry Europe 2023, Hinxton, Cambridgeshire, UK,
25.-26.5.2023
Figure 1: a) Schematic of the setup inside the µCT scanner. The object of interest
is mounted onto a rotational disk which is placed between X-Ray source and
detector. b) Process of the used image analysis: the projection images are
reconstructed to 3D slices, which are then segmented to extract 3D information
about the bubble formation.
Figure 2: The maximum bubble diameter dmax, the maximum bubble length lmax,
the maximum area Amax, and the volume of the dispersed phase Vdisp are plotted
against the dimensionless time t* for six different states during bubble formation
in rectangular (grey square) and circular capillaries (black circle).
Contacts:
bastian.oldach@tu-dortmund.de
norbert.kockmann@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 13
Smart Image Sensor for Liquid-liquid Systems
More process information for efficient and reliable process control
Inga Burke, Ahmed S. Youssef, Karthik Mannil, Katharina Schmidt, Norbert Kockmann
Smart sensor development for online process monitoring is a growing trend in the process industry. Image analysis offers an
effective instrument to analyze product properties during processes and benefits from the fast development of AI-based
object detection methods. To use image recognition methods, an optical access to the process of interest is necessary.
Therefore, a modular, optical measurement flow cell is designed to capture droplet images during an emulsification process.
Automated process control using an AI-based image analysis method is developed and validated for a final design.
Optical methods are a common tool to analyze critical
quality attributes (CQA) such as the droplet size distribution (DSD) of emulsification processes [1]. Thus, monitoring
and evaluation of the DSD and its changes during an emulsification process is an important field during process efficiency enhancement.
A prototype of an optical flow cell for online monitoring
is designed to enable optical access to an emulsification process. Possible challenges during emulsification
are high disperse phase content of liquid-liquid systems
as well as small droplets. To overcome those challenges,
the design of the optical flow cell is based on a modular
approach, which enable an adaption of the flow cell concerning the liquid-liquid system. Rapid prototyping of different optical measurement flow cells was realized using
SLA-3D printing, which provides flexible design structures
and results in an optimized design [1]. The flow cell is designed and evaluated established on an iterative optimization procedure including three key factors during prototyping (device material, channel geometry, and suitability
for emulsion systems). This approach to investigate the
emulsion system optically builds the fundamental for an
AI-based image evaluation.
Smart image sensors enhance the monitoring of multiphase processes [2], such as emulsification. To automatically determine the DSD within the emulsification process,
an AI application using different Deep Learning (DL) approaches (YOLOv4 and Mask RCNN) is developed to infer
information on how to control the process more efficiently [3]. Figure 1 illustrates the vision-based deep learning
framework, incorporating object detection and data processing, which extracts meaningful features from image
datasets.
The monitoring of the emulsification process is carried out
using the modular, optical flow cell. The captured images
are used as the input of the different models. The extracted image information, such as the phase fraction of the
used process and the droplet sizes, are used to improve
process understanding [4]. Two different AI models for
droplet size determination were tested, optimized, and
validated. Experimental investigations show that the optical, AI-based evaluation of the droplet size distribution is
performable also for higher dispersed phase fractions as
well as for droplet sizes of 5 to 100 µm. The final YOLOv4
model is robust and trustworthy for the tested application
range. This optical access as well as the performance of
both models show promising results and high potential for
online process monitoring in emulsification processes.
Figure 1: Workflow of the vision-based deep learning framework including process
information in the form of process images, the AI-based detection containing
classification, and two different DL approaches as well as the results in the form of
detection images and a statistical evaluation of the process [3].
Contacts:
inga.burke@tu-dortmund.de
norbert.kockmann@tu-dortmund.de
Publications:
[1] I. Burke, C. Assies, N. Kockmann, Investigation of an 3D-printed Optical
Measurement Flow Cell for Process Progress Monitoring of Liquid-Liquid
Systems, Flow Chemistry Europe 2023, Hinxton, Cambridgeshire, UK, 25.26.5.2023
[2] I. Burke, R. Dinter, B. Oldach, A. Frede, A. S. Behr, L. Neuendorf, S.
Höving, N. Kockmann, Data-Driven Flow Chemistry - Lab Automation, AI
Supported Modules, and Scale-up, Flow Chemistry Europe 2023, Hinxton,
Cambridgeshire, UK, 25.-26.5.2023, invited plenary talk
[3] I. Burke, A.S. Youssef, K. Mannil, K. Schmidt, N. Kockmann, Smart image
sensor for liquid-liquid systems, µFIP Conf. Micro Flow and Interfacial
Phenomena, Evanston, IL, USA, 18.-21.6.2023
[4] I. Burke, C. Assies, N. Kockmann, Investigation and characterization of an
3D-printed optical measurement flow cell for process progress monitoring
of liquid-liquid systems, µFIP Conf. Micro Flow and Interfacial Phenomena,
Evanston, IL, USA, 18.-21.6.2023
SCIENTIFIC HIGHLIGHTS 2023
Page 14
Quasi-Continuous Production of Solids in a Modular and Small-Scale Plant
Integrated processes for efficient particle generation, washing, and drying
Stefan Höving, Thomas Schmidt, Maximilian Peters, Hendrik Lapainis, Phil Bolien, Timo Dobler, Norbert Kockmann
Small-scale continuous apparatuses for solids production are receiving increasing interest due to the demand for the fast
market availability of specialty chemical products manufactured in integrated and modular processing plants. Relevant
unit operations span from crystallization over solid–liquid separation and filter cake washing to drying. For this purpose,
the quasi-continuous filter belt crystallizer (QCFBC) was developed and is presented here.
The functional principle of the apparatus is based on the
operation of a horizontal continuous belt filter. Here, the
process medium is separated into batch containers that
are transported along the operation direction of the plant,
covering functional modular units. The concept allows for
particle formation, filtration, washing, and drying on a single plant in order to connect the process from solutions to
a dry filter cake in a well-controlled manner. The modular
units are inter-changeable and the process can therefore
be custom-tailored to the specific needs of the substance
of interest. The process starts with suspension in the container positioned on the first (red in Figure 1) functional
modular unit. Here, the temperature of the suspension is
controlled via the functional modules. After, tcycle all the
containers travel to the next position. On the last position
(green in Figure 1), the product suspension is filtered and
the resulting filter cake is washed and dried.
Figure 1. 3D sketch of the modular filter belt apparatus with the five modular
functional modules. In the detailed view, the container lids are raised. The first four
positions (from left to right) are responsible for the cooling crystallization, while
the last container position serves for the filtration, washing, and drying step.
Publications:
[1] S. Höving, T. Schmidt, M. Peters, H. Lapainis, N. Kockmann,
Small-scale Solids Production Plant with Cooling Crystallization,
Washing, and Drying in a Modular, Continuous Plant, Processes,
11(8), 2457, 2023, doi.org/10.3390/pr11082457
[2] T. Dobler, S. Höving, C. Dreiser, M. Gleiß, M. Gröschen, A. Henkel,
M. Hörne, M. Schäfer, J. Sonnenschein, G. Wiese, K. Wohlgemuth, N.
Kockmann, H. Nirschl, From Lab to Pilot Scale: Commissioning of
an Integrated Device for the Generation of Crystals, Chem. Eng. &
Technol., 46(7), 1511-1520, 2023, doi.org/10.1002/ceat.202200616
[3] S. Höving, P. Bolien, P. Siebers, N. Kockmann, Simplified
Approach to Characterize the Cooling Crystallization in a Modular
Mini-Plant, Crystals, 13(1), 147, 2023, doi.org/10.3390/cryst13010147
[4] S. Höving, L. Neuendorf, T. Betting, N. Kockmann, Determination
of Crystal Size Distributions of Bulk Samples using MicroComputed Tomography and Artificial Intelligence; Materials, 16(3),
1002, 2023, doi.org/10.3390/ma16031002
The newly integrated unit operations, positive pressure filtration (Δpmax=0.8 bar), filter cake washing (V̇wash=55
mL•min-1), and convection drying (Tdry=60 °C) have been individually characterized and integrated into the filter apparatus that has been modified and automated for continuous operation. They were synchronized with the flexible
cooling crystallization, enabling for a seamless production
process. Sucrose in water was used as model substance
system. Long-term operations of up to 14 h, as demonstrated in Figure 2, were successfully performed with dry product filter cakes (22.64 g·h-1± 1.64 g·h-1) of constant quality
attributes (x50,3=216.095 µm±14.766 µm, span=0.347±0.109,
Yrel.=69.9 %±5 %, XRM= 1.64mg·g-1±1.38 mg·g-1).
Figure 2. Panel plot of relevant processes and product parameters of the longterm operation of the QCFBC with 20 consecutive containers in total. In (a), the
temperature curve of the four temperature modules is plotted. In (b), the pressure
during filtration, washing, drying, and the additionally integrated rinsing step (CIP),
is plotted. (c) shows the PSD for the seed crystals in red and the product crystals,
collected right before the filtration, in blue. In panel (d), the relative yield calculated
via the filter cake mass and the residual moisture of each of the product filter cake
is plotted.
Contacts:
stefan.hoeving@tu-dortmund.de
norbert.kockmann@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 15
Numerical modelling of the discharge behavior of particles from gas vessel
Simulating a daily-occurring phenomenon with sophisticated numerical methods to achieve excellent results.
Michael-David Fischer, Simon Baier, Konrad E.R. Boettcher
The characterisation of the outflow of gases from pressure tanks is a fundamental aerodynamic problem. Pressurized
tanks can be found in everyday life in many different sizes. From gas capsules, gas cartridges, and spray cans to gas
cylinders and tankers, a broad spectrum is covered. Particularly in the case of high internal pressures and flammable,
harmful or environmentally hazardous gases, the escape from pressurized containers due to leaks or failure is of safety
importance. This problem is extended if the gas flow has a particle load. Especially during the corona pandemic, the
discharge of potentially virus-laden particles when exhaled and their spread was omnipresent. As there is hardly any
knowledge about particle discharge to date, we have taken a first step and simplified the problem with a pressurized
container and uniform particle loading.
In detail, a cylindrical container with a volume of 2 m³ and
a length-to-diameter ratio of 2 is considered. The gas is
discharged from a circular opening with a diameter of 25
mm in the center of a circular surface of the cylinder. The
initial state of the problem is shown in Figure 1.
Figure 2: Representation of the initial regions from which particles with a density
of 2000 kg/m³ are discharged for different particle sizes.
Figure 3 compares the model with CFD simulations
showing deviations of -0.03 %.
Figure 1: Scale drawing of the thin-walled container. The initial state is sketched
here, in which the container contains a particle-laden gas. The particle size is not
shown to scale.
For the continuous gas phase, air, helium, hydrogen, methane and nitrogen are considered. In addition, the initial
pressure and temperature in the vessel are varied. For the
dispersed particle phase, the particle size and the particle density are varied. In addition to the CFD simulations
with ANSYS CFX, a similarity analysis of the problem was
carried out. For this purpose, the conservation equations
for mass, momentum, energy, turbulent kinetic energy and
dissipation rate were scaled and dimensionless parameters were derived. This made it possible to derive a prediction model, with which the particle discharge can be
determined quickly and accurately without having to carry
out complex numerical simulations that take several days.
The model is able to capture different gases, pressures,
temperatures and particle properties. Figure 2 shows the
initial regions from which the particles are entrained by
the gas flow and leave the container.
Figure 3: Fractions of discharged particles for each varied parameter plotted
against the particle diameter.
Contacts:
michael-david.fischer@tu-dortmund.de
simon.baier@tu-dortmund.de
konrad.boettcher@tu-dortmund.de
Publications:
M.-D. Fischer, S. Baier, K.E.R. Boettcher
Numerical modelling of the discharge behaviour of particles from a gas
vessel.
Results in Engineering, 18, 101207, (2023).
https://doi.org/10.1016/j.rineng.2023.101207
SCIENTIFIC HIGHLIGHTS 2023
Page 16
Real-World Szenario in a Laboratory Experiment on a Digital Twin to foster Work
4.0 Skills
Konrad E.R. Boettcher, Claudius Terkowsky, Marcel Schade, Dean Brandner, Sabrina Grünendahl
During the corona pandemic, the usual laboratory experiments could not be carried out. Ultra-concurrent or personal
remote labs offered a rapid solution, in which an approach was taken to digitize the usual laboratory work. A different path
was chosen here and the opportunity for a fundamental didactic redesign was seized to address learning objectives at
higher cognitive levels, to introduce constructive alignment as a framework for the instructional design of teaching-learning
units, to change the didactic setting from cookbook scripts with low competence growth to scenario-based learning with
high competence growth, to enable explorative learning and to increasingly address specific learning objectives that are
considered as future skills in life and work 4.0.
The laboratory experiment was developed in cooperation
with the Center of Higher Education on the basis of a
semi-finished VR environment for the visualization of flows
on a jet pump (see Fig 1). Using a checklist for constructive
alignment in laboratory instruction in engineering education, an endeavor was made to address as many of Feisel
and Rosa's thirteen fundamental laboratory learning objectives as possible in order to enable explorative learning.
Since the representation of the jet pump in VR corresponds to a digital twin, further learning objectives of the
future skills for life and work 4.0 were addressed. In addition to the organizational design principles of Industry 4.0,
these are skills for working autonomously on unclearly formulated problems without a clear goal or clear solution
but without much support from superiors and, for example, ethical decision-making skills.
In the final scenario, the students work in a development
department and only receive a vague work assignment by
email from their supervisor. Fulfilling the work assignments
confronts the students with an ethical problem that could
be solved with a considerable level of creativity. In order
not to overwhelm the students with the unfamiliar situation, five defined support levels were defined, whereby
only the penultimate level would correspond to a normal
laboratory experiment, as parts of a cookbook script are
distributed here. In order to strengthen the self-efficacy
and resilience of the students, reflection discussions were
held after the presentation of the results achieved. Constructive alignment must not forget to check learning objectives. To this end, a competence-oriented Moodle test
was designed. The students were able to compare this
laboratory experiment with the usual experiments (see
Fig. 2). The students rated this test significantly better in
terms of professional relevance and learning gain.
The learning objective of teamwork on a meta-cognitive level is currently being increasingly addressed. For example,
team role tests according to Belbin are carried out in order
to identify the roles the students are aiming for in order to
be able to recognize conflicts in teams at an early stage.
Figure 1. Semi-finished jet pump in VR: the measuring gauges are systematically
noisy and noisy according to the accuracy class, errors such as escaping particles
need to be analyzed and the fish at the bottom of the tank pose an ethical
problem.
Publications:
K. Boettcher et al. (2023) Developing a real-world scenario to foster
learning and working 4.0 – on using a digital twin of a jet pump
experiment in process engineering laboratory education, European
Journal of Engineering Education, 48:5, 949-971, https://doi.org/10.1
080/03043797.2023.2182184
K. Boettcher, et al. (2023) Work in Progress – Did You Check It?
Checklist for Redesigning a Laboratory Experiment in Engineering
Education Addressing Competencies of Learning and Working
4.0. In: Auer, M.E., Langmann, R., Tsiatsos, T. (eds) Open Science in
Engineering. REV 2023. Lecture Notes in Networks and Systems,
vol 763. Springer, Cham. (2023)
https://doi.org/10.1007/978-3-031-42467-0_56
Figure 2: Student responses on learning gains for this experiment (pink) compared
to usual experiments (blue) in German school grades.
Contacts:
stefan.hoeving@tu-dortmund.de
konrad.boettcher@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 17
Publications
2023
Peer-reviewed Journal Articles
• Dinter, R.; Götte, K.; Gronke, F.; Justen, L.; Brunschweiger, A.; Kockmann, N.
Development of an Automated Flow Chemistry Affinity‑Based
Purification Process for DNA‑Encoded Chemistry.
J. Flow Chem, 13, 361–373 (2023).
https://doi.org/10.1007/s41981-023-00282-0
• Bortz, M.; Dadhe, K.; Engell, S.; Gepert, V.; Kockmann, N.; MüllerPfefferkorn, R.; Schindler, T.; Urbas, L.
AI in Process Industries – Current Status and Future Prospects.
Chem. Ing. Technik, 95(7), 975-988 (2023).
https://doi.org/10.1002/cite.202200247
• Behr, A.S.; Völkenrath, M.; Kockmann, N.
Ontology extension with NLP-based concept extraction for domain
experts in catalytic sciences.
Knowledge and Information Systems, 65(12), 5503–5522 (2023).
https://doi.org/10.21203/rs.3.rs-3491129/v1
• Dobler, T.; Höving, S.; Dreiser, C.; Gleiß, M.; Gröschen, M.; Henkel, A.;
Hörne, M.; Schäfer, M.; Sonnenschein, J.; Wiese, G.; Wohlgemuth, K.;
Kockmann, N.; Nirschl, H.
From Lab to Pilot Scale: Commissioning of an Integrated Device for
the Generation of Crystals.
Chem Eng. & Technol., 46(7), 1511-1520 (2023).
https://doi.org/10.1002/ceat.202200616
• Neuendorf, L.M.; Khaydarov, V.; Schlander, C.; Kock, T.; Fischer. J.; Urbas,
L.; Kockmann, N.
Artificial Intelligence-based Module Type Package (MTP)-compatible
Smart Sensors in the Process Industry.
Chem. Ing. Technik, 95(10), 1546-1554 (2023).
https://doi.org/10.3389/fchem.2023.1244043
• Dinter, R.; Willems, S.; Nissalk, T.; Hastuerk, O.; Brunschweiger, A.;
Kockmann, N.
Development of a Microfluidic Photochemical Flow Reactor Concept
by Rapid Prototyping.
frontiers in chemistry, 11, 1244043 (2023).
https://doi.org/10.3389/fchem.2023.1244043
• Höving, S.; Schmidt, T.; Peters, M.; Lapainis, H.; Kockmann, N.
Small-scale Solids Production Plant with Cooling Crystallization,
Washing, and Drying in a Modular, Continuous Plant.
MDPI-processes, 11(8), 2457 (2023).
https://doi.org/10.3390/pr11082457
• Klose, A.; Wagner-Stürz, D.; Neuendorf, L.M.; Oeing, J.; Khaydarov, V.;
Schleehahn, M.; Kockmann, N.; Urbas, L.
Automated Evaluation of Biochemical Plant KPIs based on DEXPI
Information.
Chem. Ing. Technik, 95(7), 1165-1171 (2023).
https://doi.org/10.1002/cite.202200239
• Oeing, J.; Brandt, K.; Wiedau, M.; Tolksdorf, G.; Welscher, W.; Kockmann, N.
Graph Learning in Machine-Readable Plant Topology Data.
Chem. Ing. Technik, 95(7), 1049-1060 (2023).
https://doi.org/10.1002/cite.202200223
• Neuendorf, L.M.; Höving, S.; Bennemann, L.; Kockmann, N.
Detecting crystals in suspensions: convolutional neural networks vs. a
gravity based approach for size distribution detection.
Chem. Ing. Technik, 95(7), 1146-1153 (2023).
https://doi.org/10.1002/cite.202200235
• Oeing, J.; Holtermann, T.; Welscher, W.; Kockmann, N.
preHAZOP: Graph-based safety analysis for early integration into
automated engineering workflows.
Chem. Ing. Technik, 95(7), 1083-1095 (2023).
https://doi.org/10.1002/cite.202200222
• Neuendorf, L.M.; Hammal, Z.; Fricke, A.; Kockmann, N.
AI-based supervision for a stirred extraction column assisted with
population balance-based simulation.
Chem. Ing. Technik, 95(7), 1134-1145 (2023).
https://doi.org/10.1002/cite.202200241
• Bittorf, L.; Oeing, J.; Kock, T.; Garreis, R.; Kockmann, N.
Design of MTP services for modular downstream units and process
analytic technology following VDI/VDE/NAMUR 2658.
Chem. Eng. & Technol., 46(7), 1502-1510 (2023).
https://doi.org/10.1002/ceat.202200390
• Elhami, V.; Neuendorf, L.M.; Kock, T.; Kockmann, N.; Schuur, B.
Separation of Crotonic Acid and 2-Pentenoic Acid Obtained by
Pyrolysis of Bio-Based Polyhydroxyalkanoates Using a Spinning Band
Distillation Column.
ACS Sustain. Chem. Eng., 11(12), 4699-4706 (2023).
https://doi.org/10.1021/acssuschemeng.2c07046
• Dinter, R.; Willems, S.; Hachem, M.; Streltsova, Y.; Brunschweiger, A.;
Kockmann, N.
Development of a two-phase flow reaction system for DNA-encoded
amide coupling.
Reac. Chem. & Eng., 8, 1334-1340 (2023).
https://doi.org/10.1039/d3re00020f
• Frede, T.A.; Weber, C.; Christ, T.; Brockhoff, T.; Ludwig, D.; Kockmann, N.
Data Management of a Microcalorimeter Using a Modular OpenSource IoT Platform.
MDPI-processes, 11(1), 279 (2023).
https://doi.org/10.3390/pr11010279
• Sakthithasan, P.; Orth, L.; Venhuis, M.; Kockmann, N.
Design of a process intensified liquid-liquid extraction cell for higher
temperature and pressure.
Chem. Eng. & Technol., 46(5), 882-890 (2023).
https://doi.org/10.1002/ceat.202200550
• Höving, S.; Bolien, P.; Siebers, P.; Kockmann, N.
Simplified Approach to Characterize the Cooling Crystallization in a
Modular Mini-Plant.
MDPI-crystals, 13(1),147 (2023).
https://doi.org/10.3390/cryst13010147
• Höving, S.; Neuendorf, L.M.; Betting, T.; Kockmann, N.
Determination of Crystal Size Distributions of Bulk Samples using
Micro-Computed Tomography and Artificial Intelligence.
MDPI-materials, 16(3), 1002 (2023).
https://doi.org/10.3390/ma16031002
• Korel, L.; Yorsh, U.; Behr, A.S.; Kockmann, N.; Holeňa, M.
Text-to-Ontology Mapping via Natural Language Processing with
Application to Search for Relevant Ontologies in Catalysis.
MDPI-computers, 12, 14 (2023).
https://doi.org/10.3390/computers12010014
SCIENTIFIC HIGHLIGHTS 2023
• Schulz, L.; Stähle, P.; Reining, S.; Sawall, M.; Kockmann, N.; Röder, T.
Multivariate curve resolution for kinetic modeling and scale-up
prediction.
J. Flow Chem., 13, 13-19 (2023).
https://doi.org/10.1007/s41981-022-00252-y
• Frede, T.A.; Nikbin, N.; Kockmann, N.;
Reactor Performance Estimation in Microscale Flow Calorimeter for
Rapid Characterization of Exothermic Reactions.
J. Flow Chem., 13, 31-44 (2023).
https://doi.org/10.1007/s41981-022-00251-z
• Achternbosch, M.; Zibula, L.; Schmidt, A.; Krieger, W.; Kockmann, N.;
Strohmann, C.
Selective monosubstitution on a trichlorosilane with highly reactive
organolithium compounds in a microflow reactor.
J. Flow Chem., 13, 9-12 (2023).
https://doi.org/10.1007/s41981-022-00254-w
Peer-reviewed Conference Contributions
• Behr, A.S.; Abbaspour, E.; Rosenthal, K.; Pleiss, J.; Kockmann, N.
Ontology-Based Laboratory Data Acquisition with EnzymeML for
Process Simulation of Biocatalytic Reactors.
1st Conf. Research Data Infrastructure - CoRDI, Karlsruhe, 12.-14.9.2023.
https://doi.org/10.52825/cordi.v1i.324
• Behr, A.S.; Borgelt, H.; Petrenko, T.; Dörr, M.; Kockmann, N.
Investigating the Landscape of Ontologies for Catalysis Research
Data Management.
1st Conf. Research Data Infrastructure - CoRDI, Karlsruhe, 12.-14.9.2023.
https://doi.org/10.52825/cordi.v1i.232
• Oldach, B.; Höving, S.; Boettcher, K.E.R.; Kockmann, N.
Ultra-Concurrent Remote Laboratory for Microfluidic Applications.
20th Intl. Conf. Remote Eng. & Virtual Instrum., REV23, Thessaloniki,
Greece, 1.-3.3.2023.
https://doi.org/10.1007/978-3-031-42467-0_43
• Behr, A.S.; Neuendorf, L.M.; Sakthithasan, P.; Karan, M.; Fang, Q.;
Boettcher, K.E.R.; Terkowsky, C.; Kockmann, N.
Uniting Knowledge and Application in a Hybrid Laboratory
Experiment in Virtual Reality - A Cross-Reality Laboratory with
Applications of Artificial Intelligence for Industry 4.0.
20th Intl. Conf. Remote Eng. & Virtual Instrum., REV23, Thessaloniki,
Greece,1.-3.3.2023.
https://doi.org/10.1007/978-3-031-42467-0_26
Books & Book chapters
• Baerns, M.; Behr, A.; Brehm, A.; Gmehling, J.; Hinrichsen, K.-O.; Hofmann,
H.; Kleiber, M.; Kockmann, N.; Onken, U.; Palkovits, R.; Renken, A.; Vogt, D.
Technische Chemie.
Wiley-VCH, Weinheim, 2023.
ISBN 978-3-527-34574-8
• Kockmann, N.; Schuler, J.; Oldach, B.
X-Ray Based Investigations on Multiphase Capillary Flows.
in G.H. Yeoh, J.B. Joshi (Eds.) Handbook of Multiphase Flow Science and
Technology, SpringerNature, 2023.
https://doi.org/10.1007/978-981-4585-86-6_29-1
Page 18
2022
• Peer-reviewed Journal Articles
Frede, T.A.; Greive, M.; Kockmann, N.
Measuring Kinetics in Flow Using Isoperibolic Flow Calorimetry.
MDPI reactions, 3(4), 525-536 (2022).
https://doi.org/10.3390/reactions3040035
• Sonnenschein, J.; Hermes, M.; Höving, S.; Kockmann, N.; Wohlgemuth, K.
Population balance modeling of unstirred cooling crystallization on
an integrated belt filter.
Comp. & Chem. Eng., 167, 108024 (2022).
https://doi.org/10.1016/j.compchemeng.2022.108024
• Menke, M.J.; Behr, A.S.; Rosenthal, K.; Linke, D.; Kockmann, N.;
Bornscheuer, U.T.; Dörr, M.
Ontology development in Biocatalysis.
Chem. Ing. Technik, 94(11), 1827-1835 (2022).
https://doi.org/10.1002/cite.202200066
• de Cerqueira, R.; Bayomie, O.; Kockmann, N.; Neuendorf, L.M.; Lammers,
K.; Kornijez, I.; Kieling, S.; Sandermann, T.
Detecting flooding state in extraction columns: convolutional neural
networks vs. a white-box approach for image-based soft sensor
development.
Comp. & Chem. Eng., 164, 107904 (2022).
https://doi.org/10.1016/j.compchemeng.2022.107904
• Klose, A.; Lorenz, J.; Bittorf, L.; Stark, K.; Hoernicke, M.; Stutz, A.;
Weinhold, H.; Krink, N.; Welscher, W.; Eckert, M.; Unland, S.; Menschner,
A.; da Silva Santos, P.; Kockmann, N.; Urbas, L.
Orchestration of modular plants: Procedure and application for
orchestration engineering.
automatisierung atp, 63(9), 68-77 (2022).
https://doi.org/10.17560/atp.v63i9.2599
• Götte, K.; Dinter, R.; Justen, L.; Kockmann, N.; Brunschweiger, A.
Development of an Automatable Affinity Purification Process for
DNA-Encoded Chemistry.
ACS Omega, 7(32), 28369-28377 (2022).
https://doi.org/10.1021/acsomega.2c02906
• Neuendorf, L.M.; Baygi, F.Z.; Kolloch, P.; Kockmann, N.
Implementation of a control strategy of a stirred liquid-liquid
extraction column based on convolutional neural networks.
ACS Engineering Au, 2(4), 369-377 (2022).
https://doi.org/10.1021/acsengineeringau.2c00014
• Sakthithasan, P.; Gerdes, N.; Venhuis, M.; Kockmann, N.
Investigation of strong asymmetric pulsation patterns in a stirredpulsed extraction measurement cell.
Chem. Eng. Proc - PI, 180, 108757 (2022).
https://doi.org/10.1016/j.cep.2021.108757
• Oeing, J.; Welscher, W.; Krink, N.; Jansen, L.; Henke, F.; Kockmann, N.
Using artificial intelligence to support the drawing of piping and
instrumentation diagrams in DEXPI standard.
Digital Chemical Engineering, 4, 100038 (2022).
https://doi.org/10.1016/j.dche.2022.100038
• Markaj, A.; Fay, A.; Kockmann, N.
Definition, characterization, and modeling of hybrid modularmonolithic process plants.
Chem. Ing. Technik, 94(8), 1117-1130 (2022).
https://doi.org/10.1002/cite.202200048
• Schuler, J.; Herath, J.; Kockmann, N.
X-ray based Tomographic Imaging for the Investigation of Laminar
Mixing in Capillaries.
Chem. Eng. & Technol., 45(7), 1247-1254 (2022).
https://doi.org/10.1002/ceat.202100530
SCIENTIFIC HIGHLIGHTS 2023
Page 19
• Höving, S.; Oldach, B.; Kockmann, N.
Cooling Crystallization with Complex Temperature Profiles on a
Quasi-Continuous and Modular Plant.
MDPI processes, 10(6) 1047 (2022).
https://doi.org/10.3390/pr10061047
2021
• Höving, S.; Bobers, J.; Kockmann, N.
Open-source multi-purpose sensor for measurements in continuous
capillary flow.
J. Flow Chem., 12, 185-196 (2022).
https://doi.org/10.1007/s41981-021-00214-w
• Oeing, J.; Neuendorf, L.M.; Bittorf, L.; Krieger, W.; Kockmann, N.
Flooding Prevention in Distillation and Extraction Columns with Aid of
Machine Learning Approaches.
Chem. Ing. Technik, 93(12), 1917-1929 (2021).
https://doi.org/10.1002/cite.202100051
• Grühn, J.; Behr, A.S.; Rosenthal, K.; Kockmann, N.
From coiled flow inverter to stirred tank reactor - Bioprocess
development and ontology design.
Chem. Ing. Technik, 94 (6), 852-863 (2022).
https://doi.org/10.1002/cite.202100177
• Wiedau, M.; Tolksdorf, G.; Oeing, J.; Kockmann, N.
Towards a systematic data harmonization to enable AI application in
the process industry.
Chem. Ing. Technik, 93(12), 2105-2115 (2021).
https://doi.org/10.1002/cite.202100203
• Frede, T.A.; Maier, M.; Kockmann, N.; Gruber-Wölfler, H.
Advances in continuous flow calorimetry.
Org. Proc. R&D, 26(2), 267-277 (2022).
https://doi.org/10.1021/acs.oprd.1c00437
• Oeing, J.; Henke, F.; Kockmann, N.
Machine Learning based suggestions of separation units for process
synthesis in process simulation.
Chem. Ing. Technik, 93(12), 1930-1936 (2021).
https://doi.org/10.1002/cite.202100082
• Bobers, J.; Hahn, L.K.; Averbeck, T.; Brunschweiger, A.; Kockmann, N.
Reaction Optimization of a Suzuki-Miyaura Cross-Coupling using
Design of Experiments.
Chem. Ing. Technik, 94(5), 780-785 (2022).
https://doi.org/10.1002/cite.202100194
• Schmalenberg, M.; Mensing, L.; Lindemann, S.; Krell, T.; Kockmann, N.
Miniaturized Draft Tube Baffle Crystallizer for Continuous Cooling
Crystallization.
Chem. Eng. R&D, 178, 232-250 (2022).
https://doi.org/10.1016/j.cherd.2021.12.024
Peer-reviewed Conference Contributions
• Dinter, R.; Helwes, L.; Pillath, M.; Kockmann, N.
Electrical Conductivity Sensor with Open-Source Hardware for the
Microfluidic Determination of Reaction Parameters.
16. Dresdner-Sensor Symposium, 5.-7.12.2022.
https://doi.org/10.5162/16dss2022/P03
• Neuendorf, L.M.; Müller, P.; Bergeest, C.; Meijer, A.; Schlander, C.;
Kockmann, N.
Künstliche Intelligenz (KI)-basierte optische Sensorik für flüssigflüssig Systeme.
16. Dresdner-Sensor Symposium, 5.-7.12.2022.
https://doi.org/10.5162/16dss2022/P50
• Burke, I.; Youssef, A.S.; Kockmann, N.
Design of an AI-supported Sensor for Process Relevant Parameters in
Emulsification Processes.
16. Dresdner-Sensor Symposium, 5.-7.12.2022.
https://doi.org/10.5162/16dss2022/P48
• Dinter, R.; Willems, S.; Hachem, M.; Mittelstädt, M.; Brunschweiger, A.;
Kockmann, N.
Two-Phase Flow Reaction System for Amide Coupling Towards
Automated DNA-Encoded Chemistry.
ProcessNet Annual Meeting, Aachen, 12.-15.09.2022.
https://doi.org/10.1002/cite.202255228
Books & Book articles
• Kockmann, N.; Agar, D.W.
Liquid-Liquid Processes - Mass Transfer Processes and Chemical
Reactions.
in V. Ranade, R. Utikar (eds.) Multiphase Flows for Process Industries:
Fundamentals and Applications Vol. 2, Wiley-VCH, Weinheim, 2022, ISBN
978-3-527-34377-5.
https://doi.org/10.1002/9783527812066.ch5
Peer-reviewed Journal Articles
• Reichmann, F.; Herath, J.; Mensing, L.; Kockmann, N.
Gas-liquid mass transport intensification for bubble breakup
employing micronozzles.
J. Flow Chem., 11(3), 429-444 (2021).
https://doi.org/10.1007/s41981-021-00180-3
• Frede, T.A.; Dietz, M.; Kockmann, N.
Software-Guided Microscale Flow Calorimeter for Efficient
Acquisition of Thermokinetic Data.
J. Flow Chem., 11(3), 321-332 (2021).
https://doi.org/10.1007/s41981-021-00145-6
• Schmalenberg, M.; Weick, L.; Kockmann, N.
Nucleation for Continuous Flow Cooling Sonocrystallization for
Coiled Capillary Crystallizers.
J. Flow Chem., 11(3), 303-319 (2021).
https://doi.org/10.1007/s41981-020-00138-x
• Fath, V.; Lau, P.; Greve, C.; Weller, P.; Kockmann, N.; Röder, T.
Simultaneous self-optimisation of yield and by-product formation
through successive combination of inline FT-IR spectroscopy and
online mass spectrometry.
J. Flow Chem., 11(3), 285 – 302 (2021).
https://doi.org/10.1007/s41981-021-00140-x
• Schuler, J.; Herath, J.; Kockmann, N.
3D Investigation of Laminar Mixing and Diffusion in Helically Coiled
Capillaries by Micro-Computed Tomography.
J. Flow Chem., 11(3), 217-222 (2021)
https://doi.org/10.1007/s41981-021-00161-6
• Kulkarni, A.; Hartman, R.; Kockmann, N.
Editorial of Special Issue on Engineering Aspects in Flow Chemistry.
J. Flow Chem., 11(3), 211-212 (2021).
https://doi.org/10.1007/s41981-021-00197-8
• Bittorf, L.; Pathak, K.; Kockmann, N.
Spinning band distillation column – rotating element design and
vacuum operation.
Ind.&Eng. Chem. Res., 60(30), 10854-10862 (2021).
https://doi.org/10.1021/acs.iecr.1c01326
• Wulf, C.; Beller, M.; Boenisch, T.; Deutschmann, O.; Hanf, S.; Kockmann,
N.; Kraehnert, R.; Oezaslan, M.; Palkovits, S.; Schimmler, S.; Schunk, S.A.;
Wagemann, K.; Linke, D.
A Unified Research Data Infrastructure for Catalysis Research Challenges and Concepts.
ChemCatChem, 13(14), 3223-3236 (2021).
https://doi.org/10.1002/cctc.202001974R2
SCIENTIFIC HIGHLIGHTS 2023
• Bittorf, L.; Böttger, N.; Neumann, D.; Winter, A.; Kockmann, N.
Characterization of an automated spinning band column as a module
for laboratory distillation.
Chem. Eng. & Technol., 44(9), 1660-1667 (2021).
https://doi.org/10.1002/ceat.202000602
• Schmalenberg, M.; Kreis, S.; Weick, L.; Haas, C.; Sallamon, F.; Kockmann, N.
Continuous Cooling Crystallization in a Coiled Flow Inverter
Crystallizer Technology—Design, Characterization, and Hurdles.
MDPI-processes, 9, 1537 (2021).
https://doi.org/10.3390/pr9091537
• Klement, T.; Hanf, S.; Kockmann, N.; Wolff, F.; Schunk, S.A.; Röder, T.
Oscillating droplet reactor – Towards Kinetic Screening for
Heterogeneous Catalysis in Hydrogenation Reaction.
Reac. Chem. Eng., 6, 1023-1030 (2021).
https://doi.org/10.1039/D0RE00466A
• Bamberg, A.; Bortz, M.; Kockmann, N.; Bröcker, S.; Urbas, L.
The Digital Twin – Your ingenious companion for process engineering
and smart production.
Chem. Eng.&Technol., 44(6), 954-961 (2021).
https://doi.org/10.1002/ceat.202000562
• Frede, T.A.; Burke, I.; Kockmann, N.;
Software-guided Microfluidic Reaction Calorimeter Based on
Thermoelectric Modules.
Chem. Ing. Technik, 93(5), 802-808 (2021).
https://doi.org/10.1002/cite.202000223
• Klement, T.; Kockmann, N.; Schwede, C.; Röder, T.
Kinetic measurement of acryl acid polymerization at high
concentrations under nearly isothermal conditions in a pendula slug
flow reactor.
Ind. Eng. Chem. Res., 60(11), 4240-4250 (2021).
https://doi.org/10.1021/acs.iecr.0c04732
• Grühn, J.; Vogel, M.; Kockmann, N.
Digital Image Processing of Gas-Liquid Reactions in Coiled
Capillaries.
Chem. Ing. Technik, 93(5), 825-829 (2021).
https://doi.org/10.1002/cite.202000240
• Bobers, J.; Forys, E.; Oldach, B.; Kockmann, N.
Application of Polyimide-based Microfluidic Devices on Acidcatalyzed Hydrolysis of Dimethoxypropane.
Chem. Ing. Technik, 93(5), 796-801 (2021).
https://doi.org/10.1002/cite.202000224
• Schmalenberg, M.; Frede, T.A.; Mathias, C.; Kockmann, N.
Efficient Short-cut Method for Determining the Process Window in
Stirred-pulsed Extraction Columns.
Chem. Ing. Technik, 93(3), 466-472 (2021).
https://doi.org/10.1002/cite.202000066
• Schuler, J.; Neuendorf, L.M.; Petersen, K.; Kockmann, N.
Micro-Computed Tomography for the 3D Time-Resolved Investigation
of Monodisperse Droplet Generation in a Co-Flow Setup.
AIChE J., 67(2) e17111 (2021).
https://doi.org/10.1002/aic.17111
Page 20
Peer-reviewed conference Contributions
• Horsch, M.T.; Petrenko, T.; Kushnarenko, V.; Schembera, B.; Wentzel, B.;
Behr, A.S.; Kockmann, N.; Schimmler, S.; Bönisch, T.
Interoperability and architecture requirements analysis and metadata
standardization for a research data infrastructure in catalysis.
Oral presentation, DACOMSIN, 26.10.2021.
https://doi.org/10.1007/978-3-031-12285-9_10
Book chapters
• Schlüter, M.; Kexel, F.; von Kameke, A.; Hoffmann, M.; Herres-Pawlis, S.;
Klüfers, P.; Oßberger, M.; Turek, S.; Mierka, O.; Kockmann, N.; Krieger, W.
Visualization and Quantitative Analysis of Consecutive Reactions in
Taylor Bubble Flows.
pp 507-543 in: Schlüter, M.; Herres-Pawlis, S.; Nieken, U. (Eds.) Reactive
Bubble Flow. Fluid Mechanics and Its Applications, vol 128. Springer,
Cham, 2021.
https://doi.org/10.1007/978-3-030-72361-3_21
• Kockmann, N.
Historischer Abriss zur Entstehung und Entwicklung der Chemischen
Reaktionstechnik.
in: Reschetilowski, W. (Ed.) Handbuch Chemische Reaktoren, Springer,
Berlin, 2021.
https://doi.org/10.1007/978-3-662-56444-8_1-2
SCIENTIFIC HIGHLIGHTS 2023
Page 21
SCIENTIFIC HIGHLIGHTS 2023
Plant and Process Design (APT)
Page 22
SCIENTIFIC HIGHLIGHTS 2023
Page 23
Modeling of Continuous Slug Flow Cooling Crystallization towards
Pharmaceutical Application
Importance of particle suspension and hydrodynamics for understanding slug flow crystallization.
Anne Cathrine Kufner, Michael Rix, Nico Westkämper, Henrik Bettin, Kerstin Wohlgemuth
The rising trend towards continuous production in the field of small-scale crystallization has generated numerous
concepts for apparatuses for the production of active pharmaceutical ingredients (API). One such apparatus is the Slug
Flow Crystallizer (SFC), in which a flow segmentation offers advantages such as narrow residence time distributions (RTD),
intensified mixing, heat exchange and enhanced particle suspension. To date, realization and process understanding
of crystallization inside the SFC required extensive experimental effort. Therefore, a mechanistic model considering
hydrodynamics of slug flow, energy and mass balances as well as crystallization phenomena growth and agglomeration
inside the apparatus was developed. Its purpose is to facilitate transfer of new substance systems to the apparatus
by improving process understanding, estimation of the effects of operating parameters on target properties and the
prediction of crystallization behavior with minimal experimental effort.
The general setup of the SFC is shown schematically in
Figure 1. In the slug formation zone at the inlet of the apparatus a flow segmentation into slugs of seeded solution
and synthetic air is achieved. These slugs pass the tempered growth zone at the end of which an image analysis
allows for the determination of slug lengths, slug length
distributions and crystal suspension state to ensure ideal
growth conditions.
As shown in Figure 2 the resulting model is capable of providing a satisfactory calculation of all considered experiments as it provides calculations of residence time, concentration decrease and significant crystal diameters
within a ±20 % confidence interval thereby helping in enabling robust and long-term stable operation of the SFC
while laying the foundation towards automation of the apparatus [2].
Figure 1: Schematic setup of the slug flow crystallizer.
Despite efforts to describe crystallization behavior inside
SFCs, until now no published model has incorporated
the hydrodynamics of slug flow, namely the influence of
pressure drop, slug length and residence time decrease
through gas expansion. Additionally, a satisfactory prediction of agglomeration could not be performed using existing empirical kernels.
Therefore a novel model is presented which is composed
of crystallization kinetics, slug flow hydrodynamics as well
as mass and energy balances. The crystallization kinetics
include a growth and a mechanistic, fitted agglomeration
kernel which accounts for the degree of suspension of
particles caused by secondary Taylor vortices inside the
slugs and is based upon previous work [1]. The additional
calculation of slug flow hydrodynamics enables the determination of residence time as a result of acceleration by
gas expansion while the energy balance allows for a description of the degressive temperature profile.
Figure 2: Parity plots comparing the calculated and measured (a) residence time
within the SFC; (b) the concentration decreases over the SFC length due to crystal
growth; and (c) median particle size d50 of the particle size distribution using a
mechanistic agglomeration kernel.
Contact:
kerstin.wohlgemuth@tu-dortmund.de
Publications:
[1] Kufner, A.C.; Westkämper, N.; Bettin, H.; Wohlgemuth, K., Prediction of
Particle Suspension State for Various Particle Shapes Used in Slug Flow
Crystallization. Chem. Engineering 2023, 7 (2), 34. https://doi.org/10.3390/
chemengineering7020034
[2] Kufner, A.C.; Rix, M.; Wohlgemuth, K.; Modeling of continuous slug flow
cooling crystallization towards pharmaceutical applications. Processes
2023, 11(9), 2637. https://doi.org/10.3390/pr11092637
SCIENTIFIC HIGHLIGHTS 2023
Page 24
End-to-End Continuous Small-Scale Drug Substance Manufacturing: From
Continuous in-situ Nucleator to Free-Flowing Crystalline Particles
Anne Cathrine Kufner, Marc Meier and Kerstin Wohlgemuth
In the evolving landscape of pharmaceutical manufacturing, a comprehensive continuous production process is being
crafted for small-scale active pharmaceutical ingredient production. This study focuses on continuous crystallization with
separate nucleation and crystal growth units, as well as continuous downstream processing, encompassing filtration,
washing, and drying until the formation of free-flowing particles. We introduce a novel continuous nucleator designed
based on solubility data and produced via 3D printing, enabling a fast and precise small-scale manufacturing of a nucleator
meeting the requirements for nucleation and for further growth processes. The nucleator was evaluated with regard to its
suitability for continuous long-term operation across various coupled crystallizers. As a practical application example, it
is connected to a slug flow crystallizer to enable high-quality continuous crystallization. Additionally, the full integration
of downstream processes using the continuous vacuum screw filter to achieve free-flowing product particles is realized.
Even under non-optimized process conditions, with the help of in-situ generation of nuclei, free-flowing product particles
were successfully obtained. This is particularly useful during drug development when no material is available for seed
addition and quickly obtain product for further characterization.
Production in the pharmaceutical industry for a smallscale production (250 – 1000 kg a-1) is undergoing a turnaround in terms of processing methods. Thus, more and
more research is performed in the direction of continuous
production, which, however, brings challenges at a small
scale like this. There are already some concepts for continuous cooling crystallization and a few concepts for continuous solid-liquid separation, but there is still a lack of
suitable methods that provide continuous nucleation and,
thus, continuous in situ seeds for crystallization. Our study
introduces a novel continuous nucleator in form of a T-mixer designed based on phase diagrams and making use of
antisolvent nucleation. The suitability of the nucleator for
continuous, long-term operation in combination with various crystallizers was assessed to ensure an adequate
number of nuclei for the subsequent growth process and
substantial consumption of supersaturation, minimizing
the risk of fouling in subsequent continuous crystallizer.
Its implementation was shown for a slug flow crystallizer
(SFC) with the aim of producing high-quality product particles. Furthermore, with a connection to a continuous
vacuum screw filter (CVSF) for continuous particle isolation consisting of solid-liquid separation, washing, and
drying, the fully continuous crystal process chain up to the
achievement of free-flowing particles was completed.
The experimental results demonstrate that the fully continuous end-to-end small-scale manufacturing of
free-flowing particles is possible. High relative yields in the
crystal growth process in the SFC of approximately 80 %
are reproducibly achieved, the critical quality attributes
during CVSF operation are preserved and residual moisPublications:
Kufner, A.C.; Meier, M.; Wohlgemuth, K., End-to-End Continuous
Small-Scale Drug Substance Manufacturing: From a Continuous
In Situ Nucleator to Free-Flowing Crystalline Particles. Crystals, 13
(12), 1675 (2023).
https://doi.org/10.3390/cryst13121675
tures of around 3 % resulted with the configuration used,
despite a low, non-optimal filling degree of 5 % in the CVSF.
The modular setup of the CVSF provides the option to add
a drying module in order to further reduce the residual
moisture below 1 % and obtain dry, free-flowing particles
at the end of the integrated process. Additionally, the CVSF
offers the potential to realize higher filling degrees independent from the suspension volume flow rate and solid
loading by increasing the shaft diameter of the screw. This
will further improve the flexibility of the CVSF with regard
to compatibility with various types of continuous crystallizers and operation points.
Figure 1: Schematic of experimental setup for end-to-end continuous small-scale
manufacturing of free-flowing particles containing a continuous nucleator (T-mixer
with 90° inlet configuration) in stage 1, continuous crystallization (SFC) in stage 2,
and continuous particle isolation consisting of filtration and two-stage washing
(CVSF), as well as a heater between SFC and CVSF, in stage 3.
Contact:
kerstin.wohlgemuth@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 25
Publications
2023
• Qammar, H.; Pyka, T.; Koop, J.; Górak, A.; Schembecker, G.
Radial Temperature Profile Measurements to Understand Mass
Transfer in Rotating Packed Bed Distillation
Industrial and Engineering Chemistry Research, 62(38), 15588-15599 (2023)
doi.org/10.1021/acs.iecr.3c01068
• Loll, R.; Nordhausen, L.; Bieberle, A.; Schubert, M.; Pyka, T.; Koop, J.; Held,
Ch.; Schembecker, G.
Analysis of Flow Patterns in Structured Zickzack Packings for
Rotating Packed Beds Using γ-Ray Computed Tomography
Industrial and Engineering Chemistry Research, 62(38), 15625-15634 (2023)
doi.org/10.1021/acs.iecr.3c02252
• Koop, J.; Bera, N.; Quickert, E.; Schmitt, M.; Schlüter, M.; Held, Ch.;
Schembecker, G.
Separation of Volatile Organic Compounds from Viscous Liquids with
RPB Technology
Industrial and Engineering Chemistry Research, 62(34), 13637-13645 (2023)
doi.org/10.1021/acs.iecr.3c01597
• Pyka, T.; Ressemann, A.; Held, Ch.; Schembecker, G.; Repke, J.-U.
Impact of Vapor Bypasses on Separation Performance of Rotating
Packed Beds in Distillation
Industrial and Engineering Chemistry Research, 62(33), 13274-13279
(2023)
doi.org/10.1021/acs.iecr.3c01947
• Pyka, T.; Brunert, M.; Koop, J.; Bieberle, A.; Held, Ch.; Schembecker, G.
Novel Liquid Distributor Concept for Rotating Packed Beds
Industrial and Engineering Chemistry Research, 62(14), 5984-5994 (2023)
doi.org/10.1021/acs.iecr.3c00248
• Pyka, T.; Backhaus, V.; Held, Ch.; Schembecker, G.
Impact of Number of Rotors in Rotating Packed Beds on Separation
Performance in Distillation
Industrial and Engineering Chemistry Research (2023)
doi.org/10.1021/acs.iecr.3c03173
• Kufner, A.; Meier, M.; Wohlgemuth, K.
End-to-End Continuous Small-Scale Drug Substance Manufacturing:
From a Continuous In Situ Nucleator to Free-Flowing Crystalline
Particles
Crystals, 13(12), 1675 (2023)
doi.org/10.3390/cryst13121675
• Seifert, A.; Wegener, H.; Brühl, K.; Seidensticker, T.; Wohlgemuth, K.
Polymer-Grade Bio-Monomers from Oleochemicals by Combining
Homogeneous Catalysis and Selective Product Crystallization in an
Integrated Process
Processes, 11 (10), 2861 (2023)
doi.org/10.3390/pr11102861
• Kufner, A.; Rix, M.; Wohlgemuth, K.
Modeling of continuous slug flow cooling crystallization towards
pharmaceutical applications
Processes, 11(9), 2637 (2023)
doi.org/10.3390/pr11092637
• Seifert, A.; Wehning, A.; Gutsch, J.; Wohlgemuth, K.
Focusing impurities during inert gassing crystallization of complex
mixtures
Organic Process Research & Development, 27, 8, 1485-1498 (2023)
doi.org/10.1021/acs.oprd.3c00171
• Kufner, A.; Westkämper, N.; Bettin, H.; Wohlgemuth, K.
Prediction of Particle Suspension State for Various Particle Shapes
Used in Slug Flow Crystallization
Chem. Engineering, 7(2), 34 (2023)
doi.org/10.3390/chemengineering7020034
• Dobler, T.; Höving, S.; Dreiser, Ch.; Gleiß, M.; Gröschen, M.; Henkel, A.;
Hörne, M.; Schäfer, M.; Sonnenschein, J.; Wiese, G.; Wohlgemuth, K.;
Kockmann, N.; Nirschl, H.
From Lab to Pilot Scale: Commissioning of an Integrated Device for
the Generation of Crystals
Chemical Engineering & Technology, 46(7), 1511-1520 (2023)
doi.org/10.1002/ceat.202200616
SCIENTIFIC HIGHLIGHTS 2023
Page 26
2022
• Pyka, T.; Koop, J.; Held, Ch.; Schembecker, G.
Dry Pressure Drop in a Two-Rotor Rotating Packed Bed
Industrial an Engineering Chemistry Research, 61(46), 17156-17165 (2022)
doi.org/10.1021/acs.iecr.2c02500
• Buthmann, F.; Pley, F.; Schembecker, G.; Koop, J.
Automated Image Analysis for Retention Determination in Centrifugal
Partition Chromatography
Separations, 9(11), 358 (2022)
doi.org/10.3390/separations9110358
• Etmanski, M.; Breloer, M.; Weber, M.; Schembecker, G.; Wohlgemuth, K.
Interplay of Particle Suspension and Residence Time Distribution in a
Taylor-Couette Crystallizer
Chrystals, 12(12), 1845 (2022)
doi.org/10.3390/cryst12121845
• Seifert, A.; Simons, J.; Gutsch, J.; Wohlgemuth, K.
Inert gassing crystallization for improved product separation of
oleo-chemicals towards an efficient circular economy
Organic Process Research & Development 2/09 (2022),
doi.org/10.1021/acs.oprd.2c00312
• Kufner, A.; Krummnow, A.; Danzer, A.; Wohlgemuth, K.
Strategy for fast decision on material system suitability for
continuous crystallization inside a Slug Flow Crystallizer
Micromachines (2022)
https://www.mdpi.com/2072-666X/13/10/1795
• Sonnenschein, J.; Hermes, M.; Höving, S.; Kockmann, N.; Wohlgemuth, K.
Population balance modeling of unstirred cooling crystallization on
an integrated belt filter
Journal Computers and Chemical Engineering (2022)
10.1016/j.compchemeng.2022.108024
• Schreiber, M.; Schembecker,G.
Development of an Automated Adsorbent Selection Strategy for
Liquid–Phase Adsorption
Chemical Engineering and Technology 45, No. 6, 1124–1132 (2022)
doi.org/10.1002/ceat.202200152
• Lins, J.; Ebeling, U.; Wohlgemuth, K.
Agglomeration Kernel Determination by Combining In-Process Image
Analysis and Modeling
Crystal Growth & Design 22, 9, 5363–5374 (2022)
doi.org/10.1021/acs.cgd.2c00461
• Vondran, J.; Seifert, A.; Schäfer, K.; Laudanski, A.; Deysenroth, T.;
Wohlgemuth, K.; Seidensticker, T.
Progressing the Crystal Way to Sustainability: Strategy for Developing
an Integrated Recycling Process of Homogeneous Catalysts by
Selective Product Crystallization
Industrial & Engineering Chemistry Research 61,27,9621–9631 (2022)
doi.org/10.1021/acs.iecr.2c00476
• Sonnenschein, J.; Heming, R.; Wohlgemuth, K.
Archimedes Tube Crystallizer: Design and Operation of Continuous
Cooling Crystallization Based on First-Principle Modeling
Crystal Growth & Design 22, 9, 5272-5284 (2022)
doi.org/10.1021/acs.cgd.2c00399
• Lins, J.; Harweg, T.; Weichert, F.; Wohlgemuth, K.
Potential of Deep Learning Methods for Deep Level Particle
Characterization in Crystallization
Applied Sciences 12, 5, 2465 (2022)
doi.org/10.3390/app12052465
• Sonnenschein, J.; Wohlgemuth, K.
Archimedes tube crystallizer: Design and characterization for
small-scale continuous crystallization
Chemical Engineering Research and Design 178,488-501 (2022)
doi.org/10.1016/j.cherd.2021.12.017
• Steenweg, C.; Habicht, J.; Wohlgemuth, K.
Continuous Isolation of Particles with Varying Aspect Ratios up to
Thin Needles Achieving Free-Flowing Products
Crystals 12 (2), 137 (2022)
doi.org/10.3390/cryst12020137
SCIENTIFIC HIGHLIGHTS 2023
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2021
• Sonnenschein, J.; Friedrich, P.; Aghayarzadeh, M.; Mierka, O.; Turek, S.;
Wohlgemuth, K.
Flow Map for Hydrodynamics and Suspension Behavior in a
Continuous Archimedes Tube Crystallizer
Crystals 11, 1466 (2021)
doi.org/10.3390/cryst11121466
• Termühlen, M.; Etmanski, M.; Kryschewski, I.; Kufner, A.; Schembecker,
G.; Wohlgemuth, K.
Continuous Slug Flow Crystallization: Impact of Design and Operating
Parameters on Product Quality
Chemical Engineering Research and Design 170, 290–303 (2021)
doi.org/10.1016/j.cherd.2021.04.006
• Steenweg, C.; Kufner, A.; Habicht, J.; Wohlgemuth, K.
Towards Continuous Primary Manufacturing Processes - Particle
Design through Combined Crystallization and Particle Isolation
Processes 9, 2187 (2021)
doi.org/10.3390/pr9122187
• Lukin, I.; Pietzka, L.; Wingartz,I.; Schembecker, G.
Aroma absorption in rapeseed oil using rotating packed bed
Flavor and Fragrance Journal, 36,1,137-147 (2021)
doi.org/10.1002/ffj.3623
• Steenweg, C.; Seifert, A.; Böttger, N.; Wohlgemuth, K.
Process Intensification enabling Continuous Manufacturing
Processes using Modular Continuous Vacuum Screw Filter
Org. Process Res. Dev. 25, 11, 2525–2536 (2021)
doi.org/10.1021/acs.oprd.1c00294
• Schreiber, M.; Brunert, M; Schembecker, G.
Extraction on a Robotic Platform - Autonomous Solvent Selection
under Economic Evaluation Criteria
Chemical Engineering and Technology 44, No. 9, 1578-1584 (2021)
doi.org/10.1002/ceat.202100171
• Koop, J.; Merz,J.; Schembecker, G.
Hydrophobicity, amphilicity, and flexibility: Relation between
molecular protein properties and the macroscopic effects of surface
activity
Journal of Biotechnology 334, 11-25 (2021)
doi.org/10.1016/j.jbiotec.2021.05.002
• Termühlen, M.; Strakeljahn, B.; Schembecker, G.; Wohlgemuth, K.
Quantification and Evaluation of Operating Parameters’ Effect on
Suspension Behavior for Slug Flow Crystallization
Chemical Engineering Science 243, 116771 (2021)
doi.org/10.1016/j.ces.2021.116771
• Steenweg, C.; Seifert, A.; Schembecker, G.; Wohlgemuth, K.
Characterization of a Modular Continuous Vacuum Screw Filter for
Small-Scale Solid-Liquid Separation of Suspensions
Org. Process Res. Dev. 25, 4, 926–940 (2021)
doi.org/10.1021/acs.oprd.0c00550
• Peterwitz, M.; Schembecker, G.
Evaluating the potential for optimization of axial back mixing in
continuous pharmaceutical manufacturing
Computers and Chemical Engineering 04.02, 107251 (2021)
doi.org/10.1016/j.compchemeng.2021.107251
• Lins, J.; Heisel, S.; Wohlgemuth, K.
Quantification of internal crystal defects using image analysis
Powder Technology 377, 733-738 (2021)
doi.org/10.1016/j.powtec.2020.09.015
SCIENTIFIC HIGHLIGHTS 2023
Biomaterials and Polymer Science (BMP)
Page 28
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Catching and Releasing of Antibiotic Worm Micelles
Highly active worm micelles of amphiphilic polymer CIP conjugates can be deactivated by cross-linking
with triblockcopolymers and enzymatically reactivated.
Alina Romanovska, Martin Schmidt, Jonas Tophoven, Joerg C. Tiller
Modification of existing antibiotics towards higher activity particularly against antibiotic-resistant bacteria is a pressing
topic in medicine. Modification of the widely used antibiotic ciprofloxacin (CIP) with amphiphilic blockcopoly(2-oxazolines)
has been previously shown to activate the antibiotic against CIP resistant bacteria. Since CIP is not cleaved from the
conjugated polymer, common formulations to control the delivery of such polymer antibiotic conjugates (PACs) are not
applicable. In order to solve this problem, we have developed a novel approach to control the activity of polymer antibiotic
conjugates by formation of nanostructured nanoparticles and their disruption with the enzyme lipase.
As shown recently, the conjugation of CIP with amphiphilic
poly(2-oxazoline) (POx)-diblock copolymers results in great
activation of the antibiotic, which is due to the fact that the
conjugates enter the bacterial cells via their efflux pumps,
particularly if they form spherical or worm micelles. In order to control the activity of the worm micelles, it was presumed that cross-linking of the latter makes aggregates
that are too large and inflexible to enter the bacterial cells
anymore. Cleaving the cross-link will then fully recover the
activity (see Figure 1).
shows the highest deactivation in antibacterial activity
against the clinically relevant strain Staphylococcus aureus
of 135 compared to the free conjugate. The deactivation of
the CIP-conjugate by the triblock copolymers with a lower
PPhOx content or a shorter chain length is less pronounced,
which is most likely due to the lower stability of the aggregates. The concept is based on the idea that the structure
of the aggregates is majorly stabilized by the hydrophobic
end groups of the cross-linking triblockcopolymer. Thus
cleaving these groups might reverse the cross-linking process. The esterified triblockopolymers were nano-precipitated in water, isolated by centrifugation and suspended in
aqueous NaOH (0.03 M). The cloudy suspension was stirred
at room temperature and cleared after 2 h. The aggregates
were cleaved into worm micelles of the CIP PAC and spherical micelles originating from the ester end group cleaved
triblockcopolymers (see Figure micelles of the CIP PAC and
spherical micelles originating from the ester end group
cleaved triblockcopolymers (see Figure 2)
Figure 1: Illustration of the general concept of controlling the activity of crosslinked, antibacterial worm micelles based on CIP-based antibiotic polymer
conjugates (PAC) on a bacterial surface.
To find the best suited non-covalent cross-linker for the
POx-CIP micelles, a series of POx with two cleavable ester
end groups was synthesized. The resulting copolymers were
then codissolved with the worm micelle forming highly active CIP conjugate Me-PMOx15-b-PHeptOx16-EDA-xCIP in
ethanol in a 1:1 molar ratio (mol/mol) and then added to
thorouhgly stirred water. A successful formation of larger
aggregates is initially judged by a visible precipitation.The
aggregates with the triblockcopolymers that have PPhOx as
middle block seem to contain the unchanged worm micelles in all cases, indicating that the different polymers do
not mix and thus, the triblockcopolymer can act as crosslinker only. The triblockcopolymers with a longer hydrophobic middle block C8-PMOx10-b-PPhOx20-b-PMOx10-C8 and C8PMOx10-b-PPhOx40-b-PMOx10-C8 afford nanostructured
particles, which resemble densly cross-linked worm micelles (see Figure 2A). The aggregate of Me-PMOx15-b-PHeptOx 16-EDA-xCIP with C8-PMOx10-b-PPhOx20-b-PMOx10-C8
Figure 2: TEM image of cross-linked (A) and NaOH cleaved (B) aggregates
of CIP PAC worm micelles and triblockcopolymers.
The cleaved particles fully retained their antibacterial activity and this process was also successful in the presence
of the enzyme lipase. This shows the feasibility of the novel
concept, which might be transferable to other antibiotics
and drugs.
Contact:
joerg.tiller@tu-dortmund.de
jonas.tophoven@tu-dortmund.de
Publications:
Romanovska, A.; Schmidt, M.; Brandt, V.; Tophoven, J.; Tiller, J. C., Controlling
the function of bioactive worm micelles by enzyme-cleavable non-covalent
inter-assembly cross-linking. Journal of Controlled Release 2024, 368, 15-23.
https://doi.org/10.1016/j.jconrel.2024.02.013
SCIENTIFIC HIGHLIGHTS 2023
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Publications
2023
• Milovanovic, M.; Tabakoglu, F.; Saki, F.; Pohlkoetter, E.; Buga, D.; Brandt,
V.; Tiller, J. C.
Organic-inorganic double networks as highly permeable separation
membranes with a chiral selector for organic solvents.
Journal of Membrane Science 2023, 668, 121190.
doi.org/10.1016/j.memsci.2022.121190
2022
• Benitez-Duif, P. A.; Breisch, M.; Kurka, D.; Edel, K.; Gökcay, S.; Stangier, D.;
Tillmann, W.; Hijazi, M.; Tiller, J. C.,
Ultrastrong Poly(2-Oxazoline)/Poly(Acrylic Acid) Double-Network
Hydrogels with Cartilage-Like Mechanical Properties.
Advanced Functional Materials 2022, 32 (44), 2204837.
doi.org/10.1002/adfm.202204837
• Milovanovic, M.; Rauner, N.; Civelek, E.; Holtermann, T.; El Jid, O.; Meuris,
M.; Brandt, V.; Tiller, J. C.
Enzyme-Induced Ferrification of Hydrogels for Toughening of
Functional Inorganic Compounds.
Macromol. Mater. Eng. 2022, 307 (8), 2200051 .
https://onlinelibrary.wiley.com/doi/pdf/10.1002/mame.202200051
• Segiet, D.; Weckes, S.; Austermuehl, J.; Tiller, J. C.; Katzenberg, F.,
On the influence of the amorphous phase on the stability of crystals
in poly(cis-1,4-isoprene) networks.
doi.org/10.1002/app.53146
• Wilhelm, S. A.; Maricanov, M.; Brandt, V.; Katzenberg, F.; Tiller, J. C.,
Amphiphilic polymer conetworks with ideal and non-ideal swelling
behavior demonstrated by small angle X-ray scattering.
Polymer 2022, 242, 124582.
doi.org/10.1016/j.polymer.2022.124582
2021
• Benski, L.; Viran, I.; Katzenberg, F.; Tiller, J. C.,
Small-Angle X-Ray Scattering Measurements on Amphiphilic Polymer
Conetworks Swollen in Orthogonal Solvents.
Macromolecular Chemistry and Physics, 222 (1), 2000292 (2021).
doi.org/10.1002/macp.202000292
• Milovanovic, M.; Isselbaecher, N.; Brandt, V.; Tiller, J. C.,
Improving the Strength of Ultrastiff Organic–Inorganic DoubleNetwork Hydrogels.
Chemistry of Materials, 33 (21), 8312-8322 (2021).
doi.org/10.1021/acs.chemmater.1c02525
• Milovanovic, M.; Mihailowitsch, L.; Santhirasegaran, M.; Brandt, V.; Tiller, J. C.,
Enzyme-induced mineralization of hydrogels with amorphous
calcium carbonate for fast synthesis of ultrastiff, strong and tough
organic–inorganic double networks.
Journal of Materials Science, 56 (27), 15299-15312 (2021).
doi.org/10.1007/s10853-021-06204-6
• Niedik, C. F.; Jenau, F.; Maricanov, M.; Segiet, D.; Tiller, J. C.; Katzenberg, F.,
Improvement of high voltage direct current material properties upon
tailoring the morphology of crosslinked polyethylenes.
Polymer Crystallization, 4 (6), e10208 (2021).
doi.org/10.1002/pcr2.10208
• Romanovska, A.; Keil, J.; Tophoven, J.; Oruc, M. F.; Schmidt, M.; Breisch,
M.; Sengstock, C.; Weidlich, D.; Klostermeier, D.; Tiller, J. C.,
Conjugates of Ciprofloxacin and Amphiphilic Block Copoly(2-alkyl2-oxazolines)s Overcome Efflux Pumps and Are Active against
CIP-Resistant Bacteria.
Molecular Pharmaceutics, 18 (9), 3532-3543 (2021).
doi.org/10.1021/acs.molpharmaceut.1c00430
• Segiet, D.; Stockmann, A.; Sadowski, J.; Katzenberg, F.; Tiller, J. C.,
Insights in the Thermal Volume Transition of Poly(2-oxazoline)
Hydrogels.
Macromolecular Chemistry and Physics, 222 (18), 2100157 (2021).
doi.org/10.1002/macp.202100157
SCIENTIFIC HIGHLIGHTS 2023
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SCIENTIFIC HIGHLIGHTS 2023
Bioprocess Engineering (BPT)
Page 32
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Bivariate One Strain Many Compounds Designs Expand the Secondary Metabolite
Production Space in Corallococcus coralloides
Anton Lindig, Jenny Schwarz, Georg Hubmann, Katrin Rosenthal, Stephan Lütz
The scarcely investigated myxobacterium Corallococcus coralloides holds a large genome containing many uncharacterized
biosynthetic gene clusters (BGCs) that potentially encode the synthesis of entirely new natural products. Despite the
genomic potential, finding suitable cultivation conditions to trigger the production of new secondary metabolites (SMs)
has been challenging. To address this, we employed a bivariate one strain many compounds (OSMAC) approach, combining
two elicitors to activate BGCs and induce SM production in C. coralloides. The outcomes revealed synergistic effects
in the bivariate OSMAC designs, evident through the discovery of entirely new mass features (MFs) not observed in the
univariate OSMAC experiments. Molecular network analysis uncovered potential novel natural compounds and chemical
derivatives, such as the identification of N-acyl fatty amines and sulfur-containing natural products. This study highlights
the robust capacity of bivariate OSMAC designs to broaden the SMs repertoire of microorganisms with large genomes.
The rather unknown bacterium C. coralloides harbors a
large and fully sequenced genome of 10.08 Mbp with approximately 13.4% dedicated to the biosynthesis of SMs.
Utilizing antiSMASH bacterial version 6.1 for genome mining analysis, only 15 out of 36 BGCs could be linked to potential natural products (Figure 1). However, many of these
compounds have not yet been identified. Therefore, the
activation of the biosynthetic potential requires a novel
approach. Our strategy involves the combination of two
stimuli at once to investigate whether synergistic effects
in the SMs production of C. coralloides can be observed
using bivariate OSMAC approaches.
molecular family of 11 MFs belonging to N-acyl fatty amines
including N-pentyloctadecanamide that was only produced during cultivation in bivariate condition M9-medium supplemented with supernatant of S. griseochromogenes (Figure 2). Additional in silico fragmentation analysis
of a bivariate-specific singlet node revealed a potential
novel chemical structure including a sulfur moiety, benzene and an oxazole substructure.
Figure 2: Molecular network and structural elucidation of new mass features in
bivariate conditions. (A) Molecular network of all detected unique MFs in bivariate
conditions and related MFs in univariate conditions. (B) Molecular family including
possible structure of N-acyl fatty amines. (C) Single ion node representing
possible novel sulfur-containing natural product.
Figure 1: Genome mining of C. coralloides using antiSMASH 6.1. The pie chart
presents the ratio of assigned and orphan BGCs. Assigned BGCs include the
natural product (NP) class, the assigned compound and the sequence similarity to
an annotated BGC in the BGC database. Identified orphan BGCs includes their NP
class and the number of detected BGCs in the whole genome.
Unique MFs were observed in all conditions including the
control condition, the univariate conditions and the bivariate conditions. The specific combination of two stimuli
resulted in the production of entirely new unique bivariate-specific MFs. When cultivated with MD1-medium containing 1% v/v Ethanol, 5 new unique MFs were produced.
In addition, M9-medium supplemented with supernatant
of Streptomyces griseochromogenes yielded in 36 MFs,
while addition of Bacillus amyloliquefaciens supernatant
resulted in 4 MFs. Molecular network analysis unveiled a
The findings from this study strongly indicate that employing a combination of multiple elicitors in OSMAC experiments clearly broadens the biosynthetic production
space, leading to an increase in the number of chemical
derivatives and the potential discovery of novel SMs.
Contacts:
anton.lindig@tu-dortmund.de
georg.hubmann@tu-dortmund.de
stephan.luetz@tu-dortmund.de
Publications:
Lindig, A.; Schwarz, J.; Hubmann, G.; Rosenthal, K.; Lütz, S.
Bivariate One Strain Many Compounds Designs Expand the
Secondary Metabolite Production Space in Corallococcus
coralloides. Microorganisms 2023, 11, 2592. https://doi.org/10.3390/
microorganisms11102592
SCIENTIFIC HIGHLIGHTS 2023
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Reaction Engineering and Comparison of Electroenzymatic and Enzymatic ATP
Regeneration Systems
Regine Siedentop, Tobias Prenzel, Siegfried R. Waldvogel, Katrin Rosenthal, Stephan Lütz
The investigation into the electrochemical regeneration of
the cofactor Adenosine-5’-triphosphate (ATP) was selected as the Front Cover in the ChemElectroChem 22/2023
issue. ATP plays an important role in many enzymatically
catalyzed reactions and a regeneration of the cofactor can
lead to an increase in performance in cell-free reaction
systems. Such an enzymatic ATP regeneration by means
of an acetate kinase and pyruvate oxidase could be coupled to an electrochemical reaction for energy supply. The
ATP-consuming reaction was compared using the developed electrochemical regeneration as well as other enzymatic regeneration systems and it shows properties and
key figures that are promising for an economic bioprocess
using regenerative and green energy to drive the electroenzymatic reactions.
TP is a key cofactor for many biocatalytic reactions, but it
is expensive and can inhibit or deplete enzymes. Therefore, in situ regeneration of ATP is desirable for improving
the performance and feasibility of biocatalytic processes.
Various enzymatic methods have been developed for ATP
regeneration, but they have limitations such as low yield or
high cost.. We aimed to establish an electrochemically
coupled ATP regeneration system by using pyruvate oxidase (POX) and acetate kinase (ACK) and expand it by adding polyphosphate kinase (PPK) to enable the phosphorylation of AMP to broaden the application ranges in
industrial bioprocesses. The new ATP regeneration system
was compared to other enzymatic methods in terms of
phosphate donor properties and biocatalytic metrics.
We used mevalonate kinase (MVK) as a model enzyme that
requires ATP for the phosphorylation of mevalonate (MVA)
to mevalonate phosphate (MVAP). To evaluate the ATP regeneration efficiency, we measured and calculated the
yield, turnover number, and turnover frequency of the reaction using different ATP regeneration systems. . We
showed that the electroenzymatic system using POX and
ACK achieved a high yield of 84% and a high turnover number of 68 for ADP, which are superior to many other enzymatic systems. Furthermore, we also showed that the regeneration system operate under mild conditions (pH 7, 30
°C) and can be coupled to a renewable energy source. We
demonstrated that the system can be extended by adding
PPK, which can phosphorylate AMP to ADP, thus increasing the efficiency and versatility of the system.
Figure 2: ATP Regeneration systems utilizing various enzymes and phosphate
donors.
We conclude that the electroenzymatic system with POX
and ACK is a promising method for ATP regeneration, as
it offers high yield, high turnover number, mild conditions,
and renewable energy integration. The novel ATP regeneration system can be applied to other biocatalytic reactions that require ATP, such as the synthesis of terpenoids,
nucleotides, or coenzymes. In the future, the system can
be further optimized by improving the electrode design,
enzyme immobilization, and reaction engineering
Figure 1: An electrochemically coupled ATP regeneration by POX and ACK for the
phosphorylation of mevalonate was established and expanded by PPK.
Publications:
Siedentop, R.; Prenzel, T.; Waldvogel, R.S.; Rosenthal, K.; Lütz, S.
Reaction Engineering and Comparison of Electroenzymatic and
Enzymatic ATP Regeneration Systems. ChemElectroChem 2023, 10,
e202300332.
https://doi.org/10.1002/celc.202300332
Contacts:
regine.siedentop@tu-dortmund.de
krosenthal@constructor.university.de
stephan.luetz@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
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Publications
2023
2022
• Siedentop R.; Prenzel T.; Waldvogel S.R.; Rosenthal K.; Lütz S.
Reaction Engineering and Comparison of Electroenzymatic and
Enzymatic ATP Regeneration Systems.
ChemElectroChem 10, e202300332 (2023).
https://doi.org/10.1002/celc.202300332
• Becker M.; Ziemińska-Stolarska A.; Markowska D.; Lütz S.; Rosenthal K.
Comparative life cycle assessment of chemical and biocatalytic
2'3'-cyclic GMP-AMP synthesis.
ChemSusChem 16, e202201629 (2022)
https://doi.org/10.1002/cssc.202201629
• Siedentop R.; Prenzel T.; Waldvogel S.R.; Rosenthal K.; Lütz S.
Reaction Engineering and Comparison of Electroenzymatic and
Enzymatic ATP Regeneration Systems. (Coverprofil)
ChemElectroChem 10, e202300587 (2023).
https://doi.org/10.1002/celc.202300587
• Vogt J.; Rosenthal K.
Validation of Easy Fabrication Methods for PDMS-Based Microfluidic
(Bio) Reactors.
Sci 4(4):36 (2022)
https://www.mdpi.com/2413-4155/4/4/36
• Lindig A.; Schwarz S.; Hubmann G.; Rosenthal K.; Lütz S.
Bivariate One Strain Many Compounds Designs Expand the
Secondary Metabolite Production Space in Corallococcus coralloides.
Microorganisms 11(10):2592 (2023).
https://doi.org/10.3390/microorganisms11102592
• Steinmann A.; Schullehner K.; Kohl A.; Dickmeis C.; Finger M.; Hubmann
G.; Commandeur U.; Girhard M.; Urlacher V.; Lütz S.
A targeted metabolomics method for extra- and intracellular
metabolite quantification covering the complete monolignol and
lignan synthesis pathway.
Metabolic Engineering Communications 15,1-12 (2022)
https://doi.org/10.1016/j.mec.2022.e00205
• Rolf J.; Handke J.; Burzinski F.; Lütz S.; Rosenthal K.
Amino acid balancing for the prediction and evaluation of protein
concentrations in cell-free protein synthesis systems.
Biotechnol. Prog. 39(6):e3373 (2023).
https://aiche.onlinelibrary.wiley.com/doi/10.1002/btpr.3373
• Siedentop R.; Siska M.; Möller N.; Lanzrath H.; von Lieres E.; Lütz S.;
Rosenthal K.
Bayesian Optimization for an ATP-Regenerating In Vitro Enzyme
Cascade.
Catalysts 13(3):468 (2023).
https://doi.org/10.3390/catal13030468
• Siedentop R.; Dziennus M.; Lütz S.; Rosenthal K.
Debottlenecking of an In Vitro Enzyme Cascade Using a Combined
Model- and Experiment-Based Approach.
Chemie Ingenieur Technik 95: 543-548 (2023).
https://doi.org/10.1002/cite.202200170
• Kruth S.; Zimmermann C.J.-M.; Kuhr K.; Hiller W.; Lütz S.; Pietruszka J.;
Kaiser M.; Nett M.
Generation of Aurachin Derivatives by Whole-Cell Biotransformation
and Evaluation of Their Antiprotozoal Properties.
Molecules 28(3):1066 (2023).
https://doi.org/10.3390/molecules28031066
• Steinmann A.; Finger M.; Nowacki C.; Decembrino D.; Hubmann G.;
Girhard M.; Urlacher V.; Lütz S.
Heterologous Lignan Production in Stirred-Tank Reactors—
Metabolomics-Assisted Bioprocess Development for an In Vivo
Enzyme Cascade.
Catalysts 12(11):1473 (2022)
https://doi.org/10.3390/catal12111473
• Menke M.; Behr A.; Rosenthal K.; Linke D.; Kockmann N.; Bornscheuer U.;
Dörr M.
Development of an Ontology for Biocatalysis.
Chemie Ingenieur Technik, 94: 1827-1835 (2022)
https://doi.org/10.1002/cite.202200066
• Rosenthal K.; Bornscheuer U.; Lütz S.
Cascades of Evolved Enzymes for the Synthesis of Complex Molecules.
Angew. Chem. Int. Ed. 61, e202208358; Angew. Chem. 134, e202208358 (2022)
https://doi.org/10.1002/anie.202208358
• Rolf J.; Ngo A.; Tischler D.; Lütz S.; Rosenthal K.
Cell-free protein synthesis for the screening of novel azoreductases
and their preferred electron donor.
ChemBioChem 23(15), e202200121 (2022)
https://doi.org/10.1002/cbic.202200121
• Kinner A., Nerke P.; Siedentop R.; Steinmetz T.; Claassen T.; Rosenthal K.;
Nett M.; Pietruszka J.; Lütz S.
Recent Advances in Biocatalysis for Drug Synthesis
Biomedicines 10(5): 964
https://doi.org/10.3390/biomedicines10050964
• Siedentop R.; Rosenthal K.
Industrially Relevant Enzyme Cascades for Drug Synthesis and Their
Ecological Assessment:
Int. J. Mol. Sci. 23(7): 3605
https://doi.org/10.3390/ijms23073605
• Grühn J.; Behr A.; Eroglu T.; Trögel V.; Rosenthal K.; Kockmann N.
From Coiled Flow Inverter to Stirred Tank Reactor – Bioprocess
Development and Ontology Design.
Chemie Ingenieur Technik 94: 852-863 (2022)
https://doi.org/10.1002/cite.202100177
• Kinner A.; Lütz S.; Rosenthal, K.
Agar Plate-Based Screening Approach for the Identification of
Enzyme-Catalyzed Oxidations.
Chemie Ingenieur Technik 94: 1853-1859 (2022)
https://doi.org/10.1002/cite.202200084
SCIENTIFIC HIGHLIGHTS 2023
2021
• Bartsch T.*; Becker M.*; Rolf J.*; Rosenthal K.; Lütz S. (*contributed equally)
Biotechnological production of cyclic dinucleotides — Challenges and
opportunities.
Biotechnology and Bioengineering 119, 677–684 (2021)
https://doi.org/10.1002/bit.28027
• Siedentop R.; Claaßen C.; Rother D.; Lütz S.; Rosenthal K.
Getting the Most Out of Enzyme Cascades: Strategies to Optimize In
Vitro Multi-Enzymatic Reactions.
Catalysts 11(10):1183 (2021)
https://doi.org/10.3390/catal11101183
• Rolf J.; Nerke P.; Britner A.; Krick S.; Lütz S.; Rosenthal K.
From Cell-Free Protein Synthesis to Whole-Cell Biotransformation:
Screening and Identification of Novel-Ketoglutarate-Dependent
Dioxygenases for Preparative-Scale Synthesis of Hydroxy-L-Lysine.
Catalysts 11(9):1038 (2021)
https://doi.org/10.3390/catal11091038
• Kinner A.; Rosenthal K.; Lütz S.
Identification and Expression of New Unspecific Peroxygenases –
Recent Advances, Challenges and Opportunities.
Front. Bioeng. Biotechnol. 9:705630 (2021)
https://doi.org/10.3389/fbioe.2021.705630
• Schmitz LM.; Hageneier F.; Rosenthal K.; Busche T.; Brandt D.; Kalinowski
J.; Lütz S.
Recombinant Expression and Characterization of Novel P450s from
Actinosynnema mirum.
Bioorganic & Medicinal Chemistry 116241 (2021)
https://doi.org/10.1016/j.bmc.2021.116241
• Becker M.; Nikel P.; Andexer JN.; Lütz S.; Rosenthal K.
A Multi-Enzyme Cascade Reaction for the Production of 2'3'-cGAMP.
Biomolecules 11(4): 590 (2021)
https://doi.org/10.3390/biom11040590
• Schmitz LM.; Kinner A.; Althoff K.; Rosenthal K.; Lütz S.
Investigation of vitamin D2 and vitamin D3 hydroxylation by Kutzneria
albida.
ChemBioChem 22, 2266 (2021)
https://doi.org/10.1002/cbic.202100027
• Schwarz J.; Hubmann G.; Rosenthal K.; Lütz S.
Triaging of Culture Conditions for Enhanced Secondary Metabolite
Diversity from Different Bacteria.
Biomolecules 11(2), 193 (2021)
https://doi.org/10.3390/biom11020193
• Becker M.; Lütz S.; Rosenthal K.
Environmental Assessment of Enzyme Production and Purification.
Molecules 26(3):573 (2021)
https://doi.org/10.3390/molecules26030573
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SCIENTIFIC HIGHLIGHTS 2023
Computational Bioengineering (CBE)
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SCIENTIFIC HIGHLIGHTS 2023
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Tailoring Chemical Reactivity on Metal Surfaces
Quantum Mechanics (QM) meets Scanning Tunneling Microscopy (STM)
Joel Mieres-Perez, Elsa Sánchez-GarcÍa
Catalysis of chemical reactions often occurs at the surface of metals. Improving our understanding of such complex
processes is key to optimize such reactions and to design new catalytic routes. By combining QM calculations, organic
synthesis (Sander, RUB) and scanning tunneling microscopy (Morgenstern, RUB), we characterized at the molecular level
complex chemical phenomena on metal surfaces, from dimerization reactions to enantioselectivity control.
C–C bond forming reactions are essential for the chemical
and pharmaceutical industry since they are critical steps
in the synthesis of a large variety of pharmaceutical and
agrochemical compounds. Transient carbenes are organic
molecules that play a key role as intermediates in these
reactions. However, in solution chemistry, the amount of
carbene molecules that effectively undergoes C–C bond
forming reactions is diminished by side reactions, for instance with solvent molecules. Therefore, the usability
of carbene dimerization as a C–C bond forming reaction
is limited. Our quantum mechanical calculations (QM),
together with the experimental work of the Sander and
Morgenstern groups at the Ruhr University Bochum (RUB),
contributed to the development of an efficient carbene
dimerization reaction by activation with a metal surface.
Diphenylcarbene (DPC), an archetypical carbene, was adsorbed on a silver surface in the presence of water to generate the C-C coupling product (Fig. 1). By using scanning
tunneling microscopy and quantum mechanical calculations we were able to effectively identify and characterize
single molecules of the key species involved in the reaction
on the surface. In contrast to the chemistry of carbenes in
solution, where the local concentration of carbenes and
thus the probability for a dimerization reaction is small, on
the surface the conditions for dimerization reactions are
much better. The first step is a proton transfer reaction
from a water molecule to the carbene, which results in the
formation of a highly reactive cation. The metal surface
induces an electron transfer reaction from the surface
to the cation, resulting in a neutral radical species that is
mobile on the surface. The lower adsorption energy of the
radical compared to that of the carbene and the cation
allows the radical to diffuse and react with other species
on the surface, producing the C-C coupling product. This
reaction only takes place if DPC is formed on the surface
in the presence of water molecules. Our work thus paves
the way for developing novel, efficient C-C coupling reactions with no precedent in liquid phase chemistry.
Another interesting result from our single molecule studies on metal surfaces is the control of chirality.
Contacts:
joel.mieresperez@tu-dortmund.de
professors.cbe.bci@tu-dortmund.de
Chirality is a property of molecules that is of key importance for catalysis, drug development, electronics, and
nanotechnology. We studied how the chirality of single
molecules of DPC bound on a metal surface can be controlled. When adsorbed on a metal surface, the rotation of
the two phenyl rings of DPC connected to the central carbene carbon results in the formation of two distinct chiral
species (enantiomers) on the surface. These species can
be interconverted by controlling the tip-molecule distance
during the scanning tunneling microscopy experiments.
Quantum mechanical calculations revealed the geometry
changes responsible for the stabilization of each of the
enantiomers. This study delivers an important way to
achieve enantioselectivity control on metal surfaces in a
precise manner.
Figure 1: C-C coupling reaction product on a silver surface. The reaction only takes
place if DPC is formed on the surface in the presence of water.
Publications:
Cao, Y.; Mieres-Perez, J.; Lucht, K.; Ulrich, I; Schweer, P.; SanchezGarcia, E., Morgenstern, K; Sander, W., C-C coupling of carbene
molecules on a metal surface in the presence of water. Journal of
the American Chemical Society 2023, 145, 21, 11544–11552.
https://doi.org/10.1021/jacs.2c12274
Cao, Y.; Mieres-Perez, J.; Rowen, J. F.; Sanchez-Garcia, E., Sander, W.;
Morgenstern, K., Chirality control of a single carbene molecule by
tip-induced van der Waals interactions. Nature Communications
2023, 14, 4500.
https://doi.org/10.1038/s41467-023-39870-y
SCIENTIFIC HIGHLIGHTS 2023
Page 40
Towards therapeutic alternatives targeting the chemokine receptor CXCR4
Biomolecular simulations enable the optimization of peptide ligands and the discovery of small
molecules with therapeutic potential
Yasser Almeida-Hernandez and Elsa Sánchez-GarcÍa
Peptides that inhibit the chemokine receptor CXCR4 have great potential as therapeutics in the treatment of cancer and
HIV infection. The present study shows that biomolecular simulations aid the engineering of more effective variants of
such peptides. These peptide derivatives have improved plasma stability and enable radio-theragnostics applications.
Furthermore, we reported how spermine, a small molecule found in human semen, acts as inhibitor of CXCR4.
The C-X-C chemokine receptor type 4 (CXCR4) is a G-protein coupled receptor involved in key processes such as
cell migration and vascularization. CXCR4 is involved in
inflammation, human immunodeficiency virus-1 (HIV-1)
infection and in cancer, with a large amount of reported cancer cases related to CXCR4. Therefore, CXCR4 is a
very important target for the pharmaceutical industry and
therapeutics targeting CXCR4 are highly sought. Due to the
presence of CXCR4 in several body tissues and the lack of
specificity of drug candidates, blocking CXCR4 may induce
severe side effects. This represents a major obstacle to
the development of anti-CXCR4 drugs. So far, the only approved antagonist of CXCR4 is Plerixafor, which has strong
side effects in cancer patients.
EPI-X4 is an endogenous peptide inhibitor of CXCR4. Using
biomolecular simulations and experimental assays (University of Ulm), we optimized EPI-X4-derived peptides. Our
work delivered peptides with plasma stability in animal
models higher than the parent compound. At the same
time, these derivatives retain the binding and antagonistic
activity of EPI-X4 against CXCR4. Our molecular modeling
showed that, despite modifications of the N-terminal residue, the peptides preserved key interactions with CXCR4.
Radio-theragnostics approaches targeting CXCR4
are very important, since they allow both imaging and
therapy of CXCR4-related tumors. Accordingly, in collaboration with experimental partners of the University of Ulm and the University of Basel, we studied EPIX4-derived candidates modified with the 177Lu-DOTA
radiotracer(1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic
Publications:
Harms, M.; Hansson, R. F.; Gilg, A.; Almeida-Hernández, Y.; et al.
Development of N-terminally modified variants of the CXCR4antagonistic peptide EPI-X4 for enhanced plasma stability. Journal
of Medicinal Chemistry 2023, 66, 22, 15189–15204.
https://doi.org/10.1021/acs.jmedchem.3c01128
Gaonkar, R. H.; Schmidt, Y. T.; Mansi, R.; Almeida-Hernández, Y.; et al.
Development of a new class of CXCR4 targeting radioligands based
on the endogenous antagonist EPI-X4 for oncological applications.
Journal of Medicinal Chemistry (Special issue “Diagnostic and
Therapeutic Radiopharmaceuticals” 2023, 66, 13, 8484–8497.
https://doi.org/10.1021/acs.jmedchem.3c00131
Harms, M.; Smith, N.; Han, M.; Groß, R.; et al. Spermine and
spermidine bind CXCR4 and inhibit CXCR4- but not CCR5-tropic
HIV-1 infection. Science Advances 2023, 9, eadf8251.
acid-177Lu). Our biomolecular modeling (Fig. 1) showed that
the modification of the peptide scaffold does not affect
the binding of the parent peptide to CXCR4.
As mentioned, the CXCR4 receptor is also related to HIV
infections. Semen is one of the main body fluids involved in
HIV transmission. Together with our experimental partners, we reported that spermine, which is a molecule found
in human semen, blocks CXCR4, decreasing HIV-1 infection
in cells. We studied the binding of spermine to CXCR4,
through extensive biomolecular simulations. Our work
showed how spermine binds to CXCR4, involving spermine’s positive charges. Our computational models also
indicated that other related molecules which are less (or
not at all) positively charged such as putrescine, ornithine
and the four-fold acetylated spermine bind less efficiently
to CXCR4, and exhibit very poor to none inhibitory effect,
which was experimentally corroborated.
Figure 1: Depiction of our computational model of CXCR4 (partially shown, cyan),
a peptide derivative of EPI-X4 (lilac) with the radiotracer (177Lu-DOTA) highlighted.
The model cellular membrane is shown in rose with oxygen atoms in red. Water
molecules are omitted in the figure for clarity.
Our work on CXCR4 inhibitors thus opens new routes for
the design and optimization of novel scaffolds for CXCR4
antagonists.
Contacts:
yasser.almeida@tu-dortmund.de
professors.cbe.bci@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 41
Publications
2023
Peer-reviewed Journal Articles
• M. Harms, R. F. Hansson, A. Gilg, Y. Almeida-Hernández, J. Löffler, A.
Rodríguez-Alfonso, M. M. W. Habib, D. Albers, N. S. Ahmed, A.H. Abadi,
G. Winter, V. Rasche, A. J. Beer, G. Weidinger, N. Preising, L. Ständker, S.
Wiese, E. Sanchez-Garcia, A. N. Zelikin, J. Münch.
Development of N-terminally modified variants of the CXCR4antagonistic peptide EPI-X4 for enhanced plasma stability.
Journal of Medicinal Chemistry, 66, 22, 15189 (2023)
https://doi.org/10.1021/acs.jmedchem.3c01128
• Y. Cao, J. Mieres-Perez, K. Lucht, I. Ulrich, P. Schweer, E. Sanchez-Garcia,
K. Morgenstern, W. Sander.
C-C coupling of carbene molecules on a metal surface in the
presence of water.
Journal of the American Chemical Society, 145, 21, 11544 (2023)
https://doi.org/10.1021/jacs.2c12274
• C. Kling, A. Sommer, Y. Almeida-Hernandez, A. Rodríguez, J. A PerezErviti, R. Bhadane, L. Ständker, S. Wiese, H. Barth, M. Pupo-Meriño, A. T
Pulliainen, E. Sánchez-García, K. Ernst.
Inhibition of pertussis toxin by human-defensins-1 and-5: Differential
mechanisms of action.
International Journal of Molecular Sciences (Special Issue Current
Advances in Peptide Inhibitors), 24 (13), 10557 (2023)
https://doi.org/10.3390/ijms241310557
• M. Harms, N. Smith, M. Han, R. Groß, P. von Maltitz, C. Stürzel, Y. B RuizBlanco, Y. Almeida-Hernández, A. Rodriguez-Alfonso, D. Cathelin, B.
Caspar, B. Tahar, S. Sayettat, N. Bekaddour, K. Vanshylla, F. Kleipass, S.
Wiese, L. Ständker, F. Klein, B. Lagane, A. Boonen, D. Schols, S. Benichou,
E. Sanchez-Garcia, J.-P. Herbeuval, J. Münch.
Spermine and spermidine bind CXCR4 and inhibit CXCR4- but not
CCR5-tropic HIV-1 infection.
Science Advances, 9, eadf8251 (2023)
https://doi.org/10.1126/sciadv.adf8251
• Y. Cao, J. Mieres-Perez, J. F. Rowen, E. Sanchez-Garcia, W. Sander, K.
Morgenstern.
Chirality control of a single carbene molecule by tip-induced van der
Waals interactions.
Nature Communications, 14, 4500 (2023)
https://doi.org/10.1038/s41467-023-39870-y
• J. Neblik, A. Kirupakaran, C. Beuck, J. Mieres Perez, F. C. Niemeyer, M.-H.
Le, U. Telgheder, J. F. Schmuck, A. Dudziak, P. Bayer, E. Sanchez-Garcia, S.
Westermann, T. Schrader.
Multivalent molecular tweezers disrupt the essential NDC80
interaction with microtubules.
Journal of the American Chemical Society, 145, 28, 15251 (2023)
https://doi.org/10.1021/jacs.3c0218
• R. H. Gaonkar, Y. T. Schmidt, R. Mansi, Y. Almeida-Hernandez, E. SanchezGarcia, M. Harms, J. Münch, M. Fani.
Development of a new class of CXCR4 targeting radioligands based
on the endogenous antagonist EPI-X4 for oncological applications.
Journal of Medicinal Chemistry (Special issue Diagnostic and
Therapeutic Radiopharmaceuticals, 66, 13, 8484 (2023)
https://doi.org/10.1021/acs.jmedchem.3c00131
• L.-R. Olari, R. Bauer, M. Gil Miró, V. Vogel, L. Cortez Rayas, R. Groß, A. Gilg,
R. Klevesath, A. A. Rodríguez Alfonso, K. Kaygisiz, U. Rupp, P. Pant, J.
Mierez-Perez, L. Steppe, R. Schäffer, L. Rauch-Wirth, C. Conzelmann, J.
A. Müller, F. Zech, F. Gerbl, J. Bleher, N. Preising, L. Ständker, S. Wiese, D.
R. Thal, C. Haupt, H. R. A. Jonker, M. Wagner, E. Sanchez-Garcia, T. Weil,
S. Stenger, M. Fändrich, J. von Einem, C. Read, P. Walther, F. Kirchhoff, B.
Spellerberg, J. Münch.
The C-terminal 32-mer fragment of hemoglobin alpha is an
amyloidogenic peptide with antimicrobial properties.
Cellular and Molecular Life Sciences, 80, 151, (2023)
https://doi.org/10.1007/s00018-023-04795-8
• H. Shahpasand-Kroner, I. Siddique, R. Malik, G. Linares, M. Ivanova, J.
Ichida, T. Weil, J. Münch, E. Sanchez-Garcia, F.-G. Klärner, T. Schrader, G.
Bitan.
Molecular tweezers – supramolecular hosts with broad-spectrum
biological applications.
Pharmacological Reviews, 75 (2), 263 (2023)
https://doi.org/10.1124/pharmrev.122.000654
SCIENTIFIC HIGHLIGHTS 2023
Page 42
2022
Peer-reviewed Journal Articles
• L. Wettstein, P. Immenschuh, T. Weil, C. Conzelmann, Y. AlmeidaHernández, M. Hoffmann, A. Kempf, I. Nehlmeier, R. Lotke, M. Petersen,
S. Stenger, F. Kirchhoff, D. Sauter, S. Pöhlmann, E. Sanchez-Garcia,
J.Münch
Native and activated antithrombin inhibits TMPRSS2 activity and
SARS-CoV-2 infection
Journal of Medical Virology, 95 (1), e28124 (2022) Journal Cover
https://doi.org/10.1002/jmv.28124
• A. Rodríguez-Alfonso, A. Heck, Y. B Ruiz-Blanco, A. Gilg, L.Ständker, S. L.
Kuan, T. Weil, E. Sanchez-Garcia, S. Wiese, J. Münch, M. Harms
Advanced EPI-X4 derivatives covalently bind human serum albumin
resulting in prolonged plasma stability.
International Journal of Molecular Sciences, 23(23), 15029 (2022)
https://doi.org/10.3390/ijms232315029
• Y. B. Ruiz-Blanco, G. Agüero-Chapin, S. Romero-Molina, A. Antunes, L.-R.
Olari, B. Spellerberg, J. Münch, E. Sanchez-Garcia
ABP-Finder: A Tool to Identify Antibacterial Peptides and the GramStaining Type of Targeted Bacteria.
Antibiotics, 11(12), 1708 (2022)
https://doi.org/10.3390/antibiotics11121708
• N. Samanta, Y. B. Ruiz-Blanco, Z. Fetahaj, D. Gnutt, C. Lantz, J. A. Loo, E.
Sanchez-Garcia, S. Ebbinghaus
Superoxide Dismutase Folding Stability as a Target for Molecular
Tweezers in SOD1-related Amyotrophic Lateral Sclerosis.
ChemBioChem, 23, e20220039 (2022)
https://doi.org/10.1002/cbic.202200396
• T. Weil, A. Kirupakaran, M.-H. Le, P. Rebmann, J. Mieres-Perez, L. Issmail, C.
Conzelmann, J. A. Müller, L. Rauch, A. Gilg, L. Wettstein, R. Groß, C. Read, T.
Bergner, S. A. Pålsson, N. Uhlig, V. Eberlein, H. Wöll, F.-G. Klärner, S. Stenger,
B. M. Kümmerer, H. Streeck, G. Fois, M. Frick, P. Braubach, A.-L. Spetz, T.
Grunwald, J. Shorter, E. Sanchez-Garcia, T. Schrader, J. Münch
Advanced Molecular Tweezers with Lipid Anchors against SARSCoV-2 and Other Respiratory Viruses.
Journal of the American Chemical Society Au, 2(9): 2187–2202 (2022)
https://doi.org/10.1021/jacsau.2c00220
• A. Bera, S. Henkel, J. Mieres-Perez, Y. Andargie Tsegaw, E. SanchezGarcia, W. Sander, K. Morgenstern.
Surface Diffusion Aided by a Chirality Change of Self-Assembled
Oligomers under 2D Confinement
Angewandte Chemie International Edition, 61, e202212245 (2022)
https://doi.org/10.1002/anie.202212245
• S. Romero-Molina, Y. B. Ruiz-Blanco, J. Mieres-Perez, M. Harms, J.
Münch, M. Ehrmann, E. Sanchez-Garcia
PPI-Affinity: A web tool for the prediction and optimization of protein
– peptide and protein – protein binding affinity.
Journal of Proteome Research, 21, 1829−1841 (2022)
https://doi.org/10.1021/acs.jproteome.2c00020
• J. Rey, M. Breiden, V. Lux, A. Bluemke, M. Steindel, K. Ripkens, B. Möllers,
K. Bravo Rodriguez, P. Boisguerin, R. Volkmer, J. Mieres-Perez, T. Clausen,
E. Sanchez-Garcia, M. Ehrmann
An allosteric HTRA1-calpain 2 complex with restricted activation profile.
Proceedings of the National Academy of Sciences, 119, 14, e2113520119
(2022)
https://doi.org/10.1073/pnas.2113520119
• M. Harms, R. F. Hansson, S. Carmali, Y. Almeida-Hernández, E. SanchezGarcia, J. Münch, A. N. Zelikin.
Dimerization of the peptide CXCR4-antagonist on macromolecular
and supramolecular protraction arms affords increased potency and
enhanced plasma stability.
Bioconjugate Chemistry, 33, 4, 594–607, (2022) Journal Cover
https://doi.org/10.1021/acs.bioconjchem.2c00034
• R. Kosinski, J. M. Perez, E.-C. Schöneweiß, Y. B. Ruiz-Blanco, I. Ponzo, K.
Bravo-Rodriguez, M. Erkelenz, S. Schlücker, G. Uhlenbrock, E. SanchezGarcia, B. Saccà.
The role of DNA nanostructures in the catalytic properties of an
allosterically regulated protease.
Science Advances, 8, 1, (2022)
https://doi.org/10.1126/sciadv.abk0425
• D. Aschmann, C. Vallet, S. K. Tripathi, Y. B. Ruiz-Blanco, M. Brabender, C.
Schmuck, E. Sanchez-Garcia, S. K. Knauer, M. Giese.
Selective Disruption of Survivin's Protein-Protein Interactions: A
Supramolecular Approach Based on Guanidiniocarbonylpyrrole.
ChemBioChem, 23, e202100618 (2022)
https://doi.org/10.1002/cbic.202100618
• K. N. Ingenbosch, J. C. Vieyto-Nuñez, Y. B. Ruiz-Blanco, C. Mayer, K.
Hoffmann-Jacobsen, E. Sanchez-Garcia.
Effect of Organic Solvents on the Structure and Activity of a Minimal
Lipase
The Journal of Organic Chemistry, 87 (3), 1669-1678 (2022)
https://doi.org/10.1021/acs.joc.1c01136
SCIENTIFIC HIGHLIGHTS 2023
2021
Peer-reviewed Journal Articles
• G. König, P. Sokkar, N. Pryk, S. Heinrich, D. Möller, G. Cimicata, D. Matzov,
P. Dietze, W. Thiel, A. Bashan, J. E. Bandow, J. Zuegg, A. Yonath, F. Schulz,
E. Sanchez-Garcia
Rational prioritization strategy allows the design of macrolide
derivatives that overcome antibiotic resistance
Proceedings of the National Academy of Sciences, 118, 46 (2021)
https://doi.org/10.1073/pnas.2113632118
• P. Sokkar, M. Harms, C. Stürzel, A. Gilg, G. Kizilsavas, M. Raasholm, N.
Preising, M. Wagner, F. Kirchhoff, L. Ständker, G. Weidinger, B. Mayer, J.
Münch, E. Sanchez-Garcia.
Computational modeling and experimental validation of the EPI-X4/
CXCR4 complex allows rational design of small peptide antagonists
Communications Biology, 4 (1), 1-13 (2021)
https://doi.org/10.1038/s42003-021-02638-5
• T. Lohmiller, S. K. Sarkar, J. Tatchen, S. Henkel, T. Schleif, A. Savitsky, E.
Sanchez-Garcia and W. Sander
Sequential hydrogen tunneling in o-tolylmethylene
Chemistry–A European Journal, 27 (71), 17873-17879 (2021)
https://doi.org/10.1002/chem.202102010
• R. Malishev, N. Salinas, J. Gibson, A. B. Eden, J. Mieres-Perez, Y. B. RuizBlanco, O. Malka, S. Kolusheva, F. G. Klarner, T. Schrader, E. SanchezGarcia, C. Wang, M. Landau, G. Bitan, and R. Jelinek.
Inhibition of Staphylococcus aureus biofilm-forming functional
amyloid by molecular tweezers
Cell Chemical Biology, 28, 1–11 (2021)
https://doi.org/10.1016/j.chembiol.2021.03.013
• M. Böhm, K. Killinger, A. Dudziak, P. Pant, K. Jänen, S. Hohoff, K. Mechtler,
M. Örd, M. Loog, E. Sanchez-Garcia and S. Westermann.
Cdc4 phospho-degrons allow differential regulation of Ame1CENP-U
protein stability across the cell cycle
eLife, 10, e67390. (2021)
https://doi.org/10.7554/eLife.67390
• J. Mieres-Perez, K. Lucht, I. Trosien, W. Sander, E. Sanchez-Garcia, and K.
Morgenstern.
Controlling reactivity—real-space imaging of a surface metal carbene
Journal of the American Chemical Society, 143 (12), 4653–4660 (2021)
Journal Cover and ACS spotlight.
https://doi.org/10.1021/jacs.0c12995
• L. Wettstein, T. Weil, C. Conzelmann, J. A. Müller, R. Groß, M.
Hirschenberger, A. Seidel, S. Klute, F. Zech, C. P. Bozzo, N. Preising, G.
Fois, R. Lochbaum, P. M. Knaff, V. Mailänder, L. Ständker, D. R. Thal, C.
Schumann, S. Stenger, A. Kleger, G. Lochnit, B. Mayer, Y. B. Ruiz-Blanco,
M. Hoffmann, K. M. J. Sparrer, S. Pöhlmann, E. Sanchez-Garcia, F.
Kirchhoff, M. Frick & J. Münch.
Alpha-1 antitrypsin inhibits TMPRSS2 protease activity and SARSCoV-2 infection
Nature Communications, 12, 1726 (2021)
https://doi.org/10.1038/s41467-021-21972-0
• A. Meiners, S. Bäcker, I. Hadrović, C. Heid, C. Beuck, Y. B. Ruiz-Blanco, J.
Mieres-Perez, M. Pörschke, J. N. Grad, C. Vallet, D. Hoffmann, P. Bayer, E.
Sánchez- García, T. Schrader & S. K. Knauer.
Specific inhibition of the Survivin–CRM1 interaction by peptidemodified molecular tweezers
Nature Communications, 12, 1505 (2021)
https://doi.org/10.1038/s41467-021-21753-9
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SCIENTIFIC HIGHLIGHTS 2023
Computational Systems Biology (CSB)
Page 44
SCIENTIFIC HIGHLIGHTS 2023
Page 45
The pseudoentropy of allele frequency trajectories, the persistence of variation,
and the effective population size
Nikolas Vellnow, Toni I. Gossmann, David Waxman
In order to understand biological evolution and its molecular basis it is essential to measure genetic variation and follow its
change over time. Here, we derive a new measure, pseudoentropy, which concisely captures variation at individual genes or
across whole genomes. We show through diffusion analysis and individual-based computer simulations that pseudoentropy
generally decreases over time, but that these trajectories can change in response to the type of selection the population
experiences. Finally, we show the applicability of pseudoentropy for real-world data by following its changes in a natural
population of the fruit fly Drosophila melanogaster. This analysis suggests selection acting on only isolated genes of the
genome while most of the genome evolves in a neutral fashion.
To concisely describe how genetic variation, at individual
loci or across whole genomes, changes over time, and to
follow transitory allelic changes, we introduce a quantity
related to entropy, that we term pseudoentropy. This quantity emerges in a diffusion analysis of the mean time a mutation segregates in a population. For a neutral locus with
an arbitrary number of alleles, the mean time of segregation is generally proportional to the pseudoentropy of initial allele frequencies. After the initial time point, pseudoentropy generally decreases (Figure 1), but other
behaviours are possible, depending on the genetic diversity and selective forces present.
Figure 2: Change in pseudoentropy simulated for a multiple loci model under
varying negative frequency dependent selection (c=0.25 to c=0.99) and varying
recombination rate (r).
Analysis of publicly available data of a natural D. melanogaster population, that had been sampled over seven
years, using a sliding-window approach, yielded considerable variation in entropy trajectories of different genomic
regions. These mostly follow a pattern that suggests a
substantial effective population size and a limited effect
of positive selection on genome-wide diversity over short
time scales (Figure 3).
Figure 1: A plot of the pseudoentropy difference over generation time. For short
time intervals it approximates a measure of the effective population size.
For a locus with two alleles, pseudoentropy and entropy
coincide, but they are distinct quantities with more than
two alleles. Thus for populations with multiple biallelic loci,
the language of entropy suffices. Then entropy, combined
across loci, serves as a concise description of genetic variation. We used individual-based simulations to explore
how this entropy behaves under different evolutionary
scenarios. In agreement with predictions, the entropy associated with unlinked neutral loci decreases over time.
However, deviations from free recombination and neutrality have clear and informative effects on the entropy’s behaviour over time (Figure 2).
Contacts:
nikolas.vellnow@tu-dortmund.de
toni.gossmann@tu-dortmund.de
Figure 3: Little change in pseudoentropy in real-world data suggests large
effective population sizes and/or the lack of selection.
Publications:
N. Vellnow, T. Goßmann, und D. Waxman, „The pseudoentropy of
allele frequency trajectories, the persistence of variation, and the
effective population size“, Biosystems, Bd. 238, Art. Nr. 105176,
März 2024, doi: 10.1016/j.biosystems.2024.105176.
SCIENTIFIC HIGHLIGHTS 2023
Publications
2023
Peer-reviewed Journal Articles
• Ord, James, Toni I. Gossmann, and Irene Adrian-Kalchhauser.
High nucleotide diversity accompanies differential DNA methylation
in naturally diverging populations.
Molecular biology and evolution 40, no. 4 (2023): msad068.
https://doi.org/10.1093/molbev/msad068
Publications (pre-print, under review)
• Chen, Yu-Chi, David LJ Vendrami, Maximilian L. Huber, Luisa EY Handel,
Christopher R. Cooney, Joseph I. Hoffman, and Toni I. Gossmann.
Phylonumtomics uncovers diverse evolutionary trajectories of
mitogenomic fossils buried in mammalian and avian genomes.
bioRxiv (2023): 2023-08.
https://doi.org/10.1101/2023.08.07.552327
• Kaiser, Marie I., Anton Killin, Annette KF Malsch, Anja-Kristin Abendroth,
Mitja D. Back, Bernhard T. Baune, Nicola Bilstein et al.
Individualisation and Individualised Science:
Integrating Disciplinary Perspectives." (2023).
https://doi.org/10.32942/X2P016
• Muenzner, Julia, Pauline Trébulle, Federica Agostini, Christoph B.
Messner, Martin Steger, Andrea Lehmann, Elodie Caudal et al.
The natural diversity of the yeast proteome reveals chromosomewide dosage compensation in aneuploids.
BioRxiv (2022): 2022-04.
https://doi.org/10.1101/2022.04.06.487392
Page 46
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SCIENTIFIC HIGHLIGHTS 2023
Solids Process Engineering (FSV)
Page 48
SCIENTIFIC HIGHLIGHTS 2023
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UV/Vis spectroscopy as a real-time release tool for pharmaceutical tablets
René Brands, Jens Bartsch, Markus Thommes
Continuous manufacturing provides several advantages compared to batch manufacturing e.g., increased product quality
or flexible scalability, and is gaining importance in the pharmaceutical industry. In particular, the implementation of
tableting in continuous plants is an important part of current research. Therefore, the acquisition of real-time data via inline monitoring of Critical Quality Attributes (CQA) through process analytical technology (PAT) tools is crucial. This study
focuses on an UV/Vis spectroscopy approach for the quantification of the Active Pharmaceutical Ingredient (API) content
in tablets. This technology is particularly advantageous here, because of a univariate data analysis based on mechanistic
models without complex data processing and statistic models like Partial Least Squares Regression.
To ensure the reliability of the UV/Vis spectroscopy method, the corresponding probe was mounted at the tablet
ejection position (Fig. 1). Thereby, measurements were
performed on the tablet sidewall at the first moment in
time at which a tablet is accessible in its final form. Experiments were conducted at two different tableting speeds
(7200 and 20000 tablets per hour). The model formulation
consisted of lactose monohydrate, theophylline monohydrate and magnesium stearate. The validation process followed the ICH Q2 guideline focusing on specificity, linearity, precision, accuracy, and range for pharmaceutical
content uniformity.
linearity (Fig. 2) was sufficient with a coefficient of determination of 0.9891 for the low throughput and 0.9936 for
the high throughput. However, the linearity in terms of coefficient of determinations increases with increasing
tableting throughput. This was attributed to the integrated tablet surface. Increasing the tableting speeds increases the integrated tablet surface and thus the measurement volume and the number of API molecules. This leads
to a more accurate mean and lower confidence interval.
Precision was assessed in terms of intra-laboratory variations. Here, the suitability was indicated by a coefficient of
variation of 6.46% and 6.34%, respectively. Accuracy was
evaluated through mean percent recovery, indicating a
higher accuracy at 20,000 tablets per hour compared to
7,200 tablets per hour. These results can be attributed to
the previously described effects of the tableting speed on
the measured tablet surface.
Figure 1: Schematic diagram of the new developed setup of in-line monitoring with
probe and compressed air, as well as a photo of the setup.
First, a data-pretreatment was performed. In order to
evaluate the diffuse reflectance spectra of solids, the
Kubelka-Munk transformation was applied. Here, scattering and absorption coefficients are taken into account.
However, no correlation between signal intensity and API
content is recognizable after the transformation. This is
due to the fact that diffuse reflectance spectra provide
information on the chemical composition and are affected by scattering effects. Especially physical properties
like surface roughness and porosity are important factors
for the scattering behavior and therefore may disguise the
information on chemical composition. In order to remove
such scattering effects, standard normal variate transformation was performed. Subsequently, a linear relationship
is recognizable.
The specificity for the chosen formulation was confirmed
as long as the absorption maxima of the excipients and
the API do not interfere with each other. Furthermore, the
Contacts:
rene.brands@tu-dortmund.de
jens.bartsch@tu-dortmund.de
markus.thommes@tu-dortmund.de
Figure 2: Linear regression for in-line determined reflectance and theophylline
weight fraction of tablets.
In conclusion, UV/Vis spectroscopy appears to be a promising alternative to the commonly used NIR and Raman
spectroscopy methods. The simplicity of the univariate
data analysis in combination with the successful validation results highlight the potential as a reliable tool for inline monitoring of tablet content uniformity in continuous
manufacturing processes.
Publications:
Brands, R.; Bartsch, J.; Thommes, M., UV/Vis spectroscopy as
an in-line monitoring tool for tablet content uniformity. Journal
of Pharmaceutical and Biomedical Analysis 2023, S. 115721, DOI:
10.1016/j.jpba.2023.115721.
SCIENTIFIC HIGHLIGHTS 2023
Page 50
Predicting Key Process Parameters in Pharmaceutical Hot Melt Extrusion
Steven Meyer, Tobias Gottschalk, Judith Winck, Markus Thommes
A significant number of drug candidates for future use show poor solubility in aqueous media. The solubility and dissolution
rate of the active pharmaceutical ingredients (APIs) can be increased by formulating them as amorphous solid dispersions
(ASDs). In this case, the API is molecularly dispersed in the amorphous form in a polymer matrix. This means that no energy is
required to break the crystal lattice and higher apparent solubilities as well as faster dissolution can be achieved resulting
in higher bioavailability. Hot melt extrusion is a manufacturing technique that is frequently used in the pharmaceutical
industry to produce ASDs. Thereby, the dissolution of the API in the polymer is highly dependent on the process conditions.
A better understanding and the ability to predict these process parameters can give advantages in process control and
reduce experimental effort during product design. Therefore, models were developed to predict key process parameters.
The dissolution of the API in the polymer during hot melt
extrusion depends on the temperature and residence
time. If these parameters are set too low, the API may not
be fully dissolved so that no ASD is formed. However, if
temperature and residence time are set too high, the risk
of degradation of the polymer and/or the API is increased.
In this study, three pharmaceutical polymers frequently used in industrial HME were processed in autogenous
extrusion mode, which means that no heat is actively removed or added externally, but heat losses through
the extruder walls occurred. During the experiments, the
throughput was varied at a constant ratio of throughput
to screw speed (specific feed load, SFL) and the impact on
temperature and residence time was investigated. Prediction models were then derived based on the results.
For the temperature prediction, a material-independent
correlation was found between the screw speed and the
die viscosity. This means that although the melt temperature differs between the materials at the same screw
speed, the viscosity is the same. Only one experimentally
determined, extruder-dependent parameter is required to
characterize the correlation. Using the Carreau-Arrhenius
approach, which describes the relationship between viscosity and temperature, the melt temperature at the die
can be predicted for any material. The models were validated by predicting the material-specific temperature
with the set of parameters of the two other used materials.
To determine the residence time distribution, the
two-compartment model, which combines the residence
time behavior of a pipe and a continuously mixing tank,
was used to represent the experimental data. The model
uses three parameters to characterize the residence time
distribution, whereby these were used as response variables in a variance analysis with the melt temperature, the
polymer type and the SFL as influencing factors. The resulting model parameters were used to calculate the residence time distribution for all experiments performed and
Publications:
Winck, J.; Gottschalk, T.; Thommes, M., Predicting Residence
Time and Melt Temperature in Pharmaceutical Hot Melt
Extrusion. Pharmaceutics 2023, 15, 1417. https://doi.org/10.3390/
pharmaceutics15051417
compared with the experimental observations, whereby
no systematic deviations were found.
Finally, design spaces were developed to provide a simple
visualization of the complex mathematical models. These
are shown in Fig. 1 and can be used intuitively to find the
appropriate operating points for the desired residence
time or temperature. With this approach, the experimental
effort required to set optimal process parameters during
melt extrusion can be greatly reduced.
Figure 1: Melt temperature (top) and residence time (bottom) as functions of
mass flow rate and screw speed for the polymer PVPVA. The color scale is melt
temperature (top) or the 10 % quantile of the residence time distribution based on
the models.
Contacts:
steven.meyer@tu-dortmund.de
judith.winck@tu-dortmund.de
markus.thommes@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
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Increased Drug Dissolution by Embedding of Micro-Particles
Anna Justen, Alina Faye Weltersbach, Gerhard Schaldach, Markus Thommes
High dissolution rates of poor water-soluble active pharmaceutical ingredients are essential for the application of these
substances into the human body. This is achieved by a low drug particle size and the embedding of these particles in a high
water soluble matrix. Therefore, a new continuous process for the production of submicron particles (0.1-1 µm) and the in
situ implementation in a molten sugar was developed. The in vitro dissolution of drug particles shows an extraordinary high
dissolution rate.
The new concept combines the generation of submicron
particles by spray drying and their continuous embedding
in a water-soluble matrix. For the generation of dry particles in the desired size range droplets with diameters of
about 2 µm are required. An ultrasonic nebulizer based
on a piezo crystal with a particularly high resonance frequency of 3.2 MHz was utilized. Due to the high resonance
frequency exceptionally small droplets with a narrow size
distribution were generated. These were carried by a carbon dioxide gas stream into the drying unit and were deposited in the precipitation unit.
The electrostatic precipitator (Fig.1) was built of stainless
steel for particle embedding into the molten sugar alcohol
xylitol, which has a melting temperature of 96 °C. Therefore, the collecting electrode was heated throughout the
process.
distance of 50 mm and a high voltage generator was used
applying negative potential of up to 20 kV.
Drug particles (celecoxib) were deposited over a period
of 8 h in a heated wall film of molten xylitol, which was
pumped in circulate.
Figure 2: In vitro dissolution of celecoxib conducted in a flow through cell with
purified water at 37 °C, (av ± min/max, n=3).
Figure 1: Technical drawing of electrostatic precipitator, completely assembled
with glass lid, diffuser opening angle φ.
A wall film of molten xylitol served as collecting electrode.
In order to create a laminar, waveless wall film a die was
designed based on the concept of flat slit extrusion dies,
which consists of a manifold or flow channel and a land
area. The design of a coat hanger die was chosen as it provides a more stable, uniform melt distribution. The melt
was pumped in a loop with a gear pump and celecoxib particles were continuously deposited into the xylitol melt.
Therefore the discharge and collecting electrode had a
Contacts:
anna.justen@tu-dortmund.de
gerhard.schaldach@tu-dortmund.de
markus.thommes@tu-dortmund.de
The drug laden solid product was characterized regarding its dissolution behavior with the USP apparatus 4 (flow
through cell), according to the procedure described in the
European Pharmacopoeia (Fig.2). Next to the solid dispersion, obtained with the melt electrostatic precipitator, a
physical mixture with comparable drug content (0.5 wt.%)
was investigated. This product showed a two-time higher
dissolution rate (t80) in comparison to a physical mixture of
both components.
The presented method was found to be suitable for the
manufacturing of solid dispersions, which show a particularly fast drug dissolution. The knowledge gained from
this study can be applied to improve other electrostatic
precipitator designs.
Publications:
Justen, A.; Weltersbach, A.F.; Schaldach, G.; Thommes, M., Design
and Characterization of a Melt Electrostatic Precipitator for
Advanced Drug Formulations. Processes 2024, 12 (100).
https://doi.org/10.3390/pr12010100
SCIENTIFIC HIGHLIGHTS 2023
Page 52
Evolutionary Optimization of Filter Media
Kevin Hoppe, Felix Giesa, Gerhard Schaldach, Markus Thommes, Damian Pieloth
Manufacturers of filter media are faced with increasingly stringent requirements for separation performance and energy
efficiency. The development of filter media tailored to specific applications currently requires considerable experimental
effort. Due to the complex structure of filter media and the multitude of influencing variables, the application of optimization
strategies is limited. To generate optimized filter structures with improved properties, a conceptual framework has been
developed based on the integration of evolutionary optimization and 1D simulation of the filter gradient structure. The
resulting filter media exhibit significantly lower increases in pressure drops compared to reference geometries.
The developed strategy
for optimizing filter media is rooted in the principles of Darwin's theory
of evolution, as observed
in nature, involving the
mutation and selection
of the best-adapted individuals (see Figure 1).
Figure 1: Simplified principle of evolutionary optimization of filter media.
The assessment of fitness is based on the separation efficiency of filters in their initial state and the increase in
pressure drop during the storage of solid particles within
the filter. The driving force behind this optimization strategy lies in generating as many descendants as possible and
inducing mutations. To facilitate this, a previously developed 1D model with low computational complexity is employed, enabling the calculation of a high number of filter
structures concerning their filtration efficiency and pressure drop. An optimization study was conducted based on
optimizing the porosity gradient.
A constant porosity across the filter thickness is considered as a reference (generation 1), and the optimization
process was tracked over approximately 10,000 generations. The evolution of the porosity gradient is depicted for
different generations in Figure 2. This illustrates the initial
random mutation of the structure, which leads to a twostage structure with increasing generations. Calculations
showed that a significantly more uniform storage of particles within the filter could be achieved. This improved utilization of the filter surface also significantly and reduced
the increase in pressure drop, as shown in Figure 3. Filtration efficiency could even be increased, highlighting the
unique potential of this strategy for managing conflicting
requirements.
Figure 3: Pressure drops of reference and optimized filter as a function of the filter
loading.
Figure 2: Evolution of filter porosity during the optimization process.
Publications:
Hoppe, K; Wischemann, L; Schaldach, G; Zielke, R; Tillmann, W;
Thommes, M; Pieloth, D, Filtration Kinetics of Depth FiltersModeling and Comparison with Tomographic Data of Particle
Depositions, Atmosphere 2023, 14-4 (640)
Hoppe, K; Giesa, F; Schaldach, G; Thommes, M; Pieloth, D,
Optimization of Filter Structures by Evolutionary Strategies
Materials Today Communications, 2024, accepted.
The strategy is versatile, capable of taking any structural
parameter of the filter medium into account. With the ability to conduct an optimization over 10,000 generations on
a standard PC within 12 hours, this approach becomes accessible to a broad user base, facilitating the personalized
selection and design of filter materials.
Contacts:
kevin.hoppe@tu-dortmund.de
damian.pieloth@tu-dortmund.de
markus.thommes@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 53
Publications
2023
• Brands, R.; Tebart, N.; Thommes, M.
UV/Vis spectroscopy as an in-line monitoring tool for tablet content
uniformity.
Journal of Pharmaceutical and Biomedical Analysis, 236 (2023).
https://doi.org/10.1016/j.jpba.2023.115721
• Mansuri, A.; Völkel, M.; Mihiranga, D.; Feuerbach, T.; Winck, J.; Vermeer, A.
W. P.; Hoheisel, W.; Thommes, M.
Predicting self-diffusion coefficients in semi-crystalline and
amorphous solid dispersions using free volume theory.
European Journal of Pharmaceutics and Biopharmaceutica, 190, 107-120
(2023).
https://doi.org/10.1016/j.ejpb.2023.07.001
• Nesges, D.; Lang, T.; Birr, Th.; Thommes, M.; Bartsch, J.
Planetary roller melt granulation (PRMG) – A new continuous method
for powder processing.
Powder Technology, 427 (2023).
https://doi.org/10.1016/j.powtec.2023.118728
• Lang, T.; Bramböck, A.; Thommes, M.; Bartsch, J.
Material Transport Characteristics in Planetary Roller Melt
Granulation.
Pharmaceutics, 15, 8 (2023).
https://doi.org/10.3390/pharmaceutics15082039
• Winck, J.; Gottschalk, T.; Thommes, M.
Predicting Residence Time and Melt Temperature in Pharmaceutical
Hot Melt Extrusion.
Pharmaceutics 15 (5), 1417 (2023).
https://doi.org/10.3390/pharmaceutics15051417
• Mansuri, A.; Völkel, M.; Feuerbach, T.; Winck, J.; Vermeer, A. W. P.;
Hoheisel, W.; Thommes, M.
Modified Free Volume Theory for Self-Diffusion of Small Molecules in
Amorphous Polymers.
Macromolecules, 56 (8), 3224-3237 (2023).
https://doi.org/10.1021/acs.macromol.2c02451
• Mansuri, A.; Münzner, Ph.; Heermant, A.; Hänsch, S.; Feuerbach, T.;
Fischer, B.; Winck, J.; Vermeer, A. W.P.; Hoheisel, W.; Böhmer, R.; Gainaru,
C.; Thommes, M.
Characterizing Phase Separation of Amorphous Solid Dispersions
Containing Imidacloprid.
Molecular Pharmaceutics, 20 (4), 2080-2093 (2023).
https://doi.org/10.1021/acs.molpharmaceut.2c01043
• Mansuri, A.; Münzner, Ph.; Heermant, A.; Patzina, F.; Feuerbach, T.; Winck,
J.; Vermeer, A. W. P.; Hoheisel, W.; Böhmer, R.; Gainaru, C.; Thommes, M.
Molecular Dynamics and Diffusion in Amorphous Solid Dispersions
Containing Imidacloprid.
Molecular Pharmaceutics, 20 (4), 2067-2079 (2023).
https://doi.org/10.1021/acs.molpharmaceut.2c01042
• Justen, A.; Kurth, Ch.; Schaldach, G.; Thommes, M.
Preparation of Micron and Submicron Particles via Spray Drying and
Electrostatic Precipitation.
Chemical Engineering and Technology, 46 (2), 343–349 (2023).
https://doi.org/10.1002/ceat.202200357
• Zimmermann, M.; Michel, F.; Bartsch, J.; Thommes, M.
A novel approach of external lubrication in a rotary tablet press using
electrostatics.
Drug Development and Industrial Pharmacy, 48, 737-744 (2023).
https://doi.org/10.1080/03639045.2023.2165662
• Pieloth, D.; Rodeck, M.; Schaldach, G.; Thommes, M.
Categorization of Sprays by Image Analysis with Convolutional
Neuronal Networks.
Chemical Engineering Technology, 46 (2), 264-269 (2023).
https://doi.org/10.1002/ceat.202200356
• Hoppe, K.; Wischemann, L.; Schaldach, G.; Zielke, R.; Tillmann, W.;
Thommes, M.; Pieloth, D.
Filtration Kinetrics of Depth Filters-Modeling and Comparison with
Tomographic Data of Particle Depositions
Atmosphere, 14 (4), 640 (2023).
https://doi.org/10.3390/atmos14040640
• Lauscher, C.; Licau, A.; Schaldach, G.; Thommes, M.
Characterization of Sprays Generated by the Expansion of Emulsions
with Liquid Carbon Dioxide
Chemical Engineering and Technology (2023).
https://doi.org/10.1002/ceat.202300261
SCIENTIFIC HIGHLIGHTS 2023
2022
2021
• Sleziona, D.; Ely, D. R.; Thommes, M.
Modeling of Particle Dissolution Behavior Using a Geometrical
Phase-Field Approach.
Molecular Pharmaceutics, 19 (11), 3749–3756 (2022).
https://doi.org/10.1021/acs.molpharmaceut.2c00214
• Mansuri, A.; Münzner, P.; Feuerbach, T.; Vermeer, A. W. P.; Hoheisel, W.;
Böhmer, R.; Thommes, M.; Gainaru, C.
The relaxation behavior of supercooled and glassy imidacloprid.
Journal of Chemical Physics 155, 174502 (2021).
https://doi.org/10.1063/5.0067404
• Gottschalk, T.; Özbay, C.; Feuerbach, T.; Thommes, M.
Predicting Throughput and Melt Temperature in Pharmaceutical Hot
Melt Extrusion.
Pharmaceutics, 14 (9), 1757 (2022).
https://doi.org/10.3390/pharmaceutics14091757
• Evers, M.; Mattusch, A.; Weis, D.; Garcia, E.; Antonyuk, S.; Thommes, M.
Elucidation of mass transfer mechanisms in pellet formation by
spheronization.
European Journal of Pharmaceutics and Biopharmaceutics 160, 92-99
(2021).
https://doi.org/10.1016/j.ejpb.2021.01.013
• Lauscher, C.; Schaldach, G.; Thommes, M.
Particle Generation with Liquid Carbon Dioxide Emulsions.
Chemical Engineering and Technology, 45 (9), 1631–1636 (2022).
https://doi.org/10.1002/ceat.202200176
• Evers, M.; Weis, D.; Antonyuk, S.; Thommes, M.
Particle movement in the spheronizer – Experimental investigations
with respect to the toroidal and poloidal direction.
Powder Technology, 404, 117452 (2022).
https://doi.org/10.1016/j.powtec.2022.117452
• Zimmermann, M.; Raffel, C.; Bartsch, J.; Thommes, M.
Simulation of Powder Flow Behavior in an Artificial Feed Frame Using
an Euler-Euler Model.
Chemical Engineering and Technology, 45 (5), 853–859 (2022).
https://doi.org/10.1002/ceat.202100580
• Wolbert, F.; Fahrig, I.-K.; Gottschalk, T.; Luebbert, C.; Thommes, M.;
Sadowski, G.
Factors Influencing the Crystallization-Onset Time of Metastable ASDs.
Pharmaceutics, 14 (2), 269 (2022).
https://doi.org/10.3390/pharmaceutics14020269
• Lauscher, C.; Schaldach, G.; Thommes, M.
An Approach for Small Droplet Production: Nebulization by
Expansion of Water/Liquid Carbon Dioxide Emulsion.
Atomization and Sprays, 32 (4), 77–93 (2022).
https://doi.org/10.1615/AtomizSpr.2022039582
• Gottschalk, T.; Grönniger, B.; Ludwig, E.; Wolbert, F.; Feuerbach, T.;
Sadowski, G.; Thommes, M.
Influence of process temperature and residence time on the
manufacturing of amorphous solid dispersions in hot melt extrusion.
Pharmaceutical Development and Technology, 27 (3), 313–318 (2022).
https://doi.org/10.1080/10837450.2022.2051549
• da Igreja, P.; Klump, D.; Bartsch, J.; Thommes, M.
Reduction of submicron particle agglomeration via melt foaming in
solid crystalline suspension.
Journal of Dispersion Science and Technology
https://doi.org/10.1080/01932691.2022.2146707
• Winck, J.; Daalmann, M.; Berghaus, A.; Thommes, M.
In-line-monitoring of solid dispersion preparation in smale scale
extrusion based on UV-vis spectroscopy.
Journal of Pharmaceutical Development and Technology
https://doi.org/10.1080/10837450.2022.2144887
Books & Book Chapters
• Bauer-Brandl, A.; Ritschel, W. A.; Thommes, M.; Warnke, G.
Die Tablette, Handbuch der Entwicklung, Herstellung und
Qualitätssicherung.
Editio Cantor Verlag, ISBN 978-3-87193-487-2, 4. Auflage (2022).
• Flügel, K.; Schmidt, K.; Mareczek, L.; Gäbe, M.; Hennig, R.; Thommes, M.
Impact of incorporated drugs on material properties of amorphous
solid dispersions.
European Journal of Pharmaceutics and Biopharmaceutics 159, 88-98
(2021).
https://doi.org/10.1016/j.ejpb.2020.12.017
• Feuerbach, T.; Thommes, M.
Design and Characterization of a Screw Extrusion Hot-End for Fused
Deposition Modeling.
Molecules 26 (3), 590 (2021).
https://doi.org/10.3390%2Fmolecules26030590
• Weis, D.; Grohn, P.; Evers, M.; Thommes, M.; García, E.; Antonyuk, S.
Implementation of formation mechanisms in DEM simulation of the
spheronization process of pharmaceutical pellets.
Powder Technology 378, Part A, 667-679 (2021).
https://doi.org/10.1016/j.powtec.2020.09.013
• Zimmermann, M.; Thommes, M.
Residence time and mixing capacity of a rotary tablet press feed frame.
Drug Development and Industrial Pharmacy 47 (5), 790–798 (2021).
https://doi.org/10.1080/03639045.2021.1934871
• da Igreja, P.; Erve, A.; Thommes, M.
Melt milling as manufacturing method for solid crystalline
suspensions.
European Journal of Pharmaceutics and Biopharmaceutics 158,
245-253 (2021).
https://doi.org/10.1016/j.ejpb.2020.11.020
• Sleziona, D.; Mattusch, A.; Schaldach, G.; Ely, D.R.; Sadowski, G.;
Thommes, M.
Determination of Inherent Dissolution Performance of Drug
Substances.
Pharmaceutics 13 (2), 146 (2021).
https://doi.org/10.3390/pharmaceutics13020146
SCIENTIFIC HIGHLIGHTS 2023
SCIENTIFIC HIGHLIGHTS 2023
Fluid Separations (FVT)
Page 56
SCIENTIFIC HIGHLIGHTS 2023
Page 57
Recent Developments in Rotating Packed Bed Technology
Nico-Joel Greven, Tobias Pyka, Rouven Loll, Christoph Held, Gerhard Schembecker
Recent advances in rotating packed bed (RPB) technology have revolutionized mass transfer efficiency and separation
performance. Still, one open question is how to efficiently feed the liquid into the RPB. A pivotal development lies in a novel
liquid distribution system, the rotating baffle distributor (RBD). This innovative distributor, leveraging rotor rotational speed
(nrot), ensures uniform liquid distribution across the rotors, a feature previously unattainable with traditional methods.
Additionally, pioneering γ-ray computed tomography (CT) techniques have been employed to scrutinize the intricate fluid
dynamics within RPBs, shedding light on liquid distribution phenomena, including the behavior of structured Zickzack
packings (ZZ packings) under varying operational conditions.
Beneficial liquid distribution is of major importance in
separation equipment, and mal-distribution must be
avoided. The effectiveness of the RBD in achieving uniform fluid distribution was investigated in detail using
high-speed camera analyses and CT scans. The results
emphasized the ability of the RBD to achieve axial and circumferential liquid distribution, even at high rotational
speeds of more than 600 rpm. Distillation experiments
with RBDs showed superior separation efficiency compared to conventional methods, especially at rotation
speeds of more than 900 rpm, highlighting the operational
advantages. These results are shown schematically in Figure 1, as well as the RBD design.
Figure 1: CAD drawings of the RBD with (a) 12 baffle plates and (b) 36 baffle plates
and schematic illustration of the theoretical stages of the rotational speed during
the distillation of ethanol water of the RBD 36 and a full-jet nozzle.
Investigations of the influence of different liquid distributors on liquid hold-up distribution within RPBs elucidated
critical factors impacting separation performance. γ-ray
CT imaging enabled non-invasive visualization of liquid
accumulation phenomena, revealing the propensity for
mal-distribution with conventional single-point full-jet
nozzles. In contrast, RBDs demonstrated enhanced liquid
distribution uniformity, mitigating the risk of mal-distribution and optimizing mass transfer efficiency. A comparison of the 12-baffle RBD, 36-baffle RBD, and single-point
full-jet (SPFJ) nozzle is illustrated in Figure 2.
Furthermore, as depicted in Figure 3, analyses of flow patterns within structured ZZ packings using Y-ray CT imaging provided insights into the interplay between rotational speed and liquid distribution uniformity. Observations
Contact:
nico.greven@tu-dortmund.de
christoph.held@tu-dortmund.de
gerhard.schembecker@tu-dortmund.de
highlighted the critical role of operational parameters in
maintaining homogeneous liquid distribution, emphasizing
the importance of optimizing parameters to maximize
mass transfer efficiency within RPBs.
These advances highlight the transformative potential of
novel liquid distribution concepts and analytical techniques to improve the performance and scalability of
RPBs and open a new era of efficiency and sustainability
of separation processes in various industrial applications.
Figure 2: Comparison of axial liquid hold-up distributions using RBD-12, RBD-36,
and SPFJ nozzle as liquid distributors for a packing height of 9 mm using different
nrot = 300 rpm and nrot = 900 rpm, V̇L = 60 l h–1, and FG = 2.3 Pa0.5.
Figure 3: Summary of axial and radial distributions of dry rotor elements and
corresponding liquid fractions in unstacked ZZ packing at rotational speeds from
300 to 1800 rpm, with air and tap water flow rates of V̇G,1 = 0.5 m3/h and V̇L,1 = 0.48
m3/h, and V̇G,3 = 1 m3/h-1 and V̇L,3 = 0.96 m3/h-1.
Publications:
Pyka, T.; Bieberle, A.; Loll, R.; Held, C.; Schubert, M.; Schembecker,
G.: Distributor Effects on Liquid Hold-Up in Rotating Packed
Beds. Ind. Eng. Chem. Res. 2024, 63 (4), 2000-2010. https://doi.
org/10.1021/acs.iecr.3c03996
Loll, R.; Nordhausen, L.; Bieberle, A.; Schubert, M.; Pyka, T.;
Koop, J.; Held, C.; Schembecker, G.: Analysis of Flow Patterns in
Structured Zickzack Packings for Rotating Packed Beds Using
Y-Ray Computed Tomography. Ind. Eng. Chem. Res. 2023, 62 (38),
15625-15634. https://doi.org/10.1021/acs.iecr.3c02252
SCIENTIFIC HIGHLIGHTS 2023
Page 58
Publications
2023
2022
• Pyka, T.; Backhaus, V.; Held, C.; Schembecker, G.
Impact of number of rotors in rotating packed beds on separation
performance in distillation.
Ind. Eng. Chem. Res. 62 (46), 19855-19861 (2023).
https://doi.org/10.1021/acs.iecr.3c03173
• Peterwitz, M.; Jodwirschat, J.; Loll, R.; Schembecker, G.
Tracking raw material flow through a continuous direct compression
line Part I of II: Residence time distribution modeling and sensitivity
analysis enabling increased process yield.
Int. J. Pharm. 614, 121467 (2022).
https://doi.org/10.1016/j.ijpharm.2022.121467
• Hubach, T.; Pillath, M.; Knaup, C.; Schlüter, S.; Held, C.
Li+ Separation from Multi-Ionic Mixtures by Nanofiltration
Membranes: Experiments and Modeling.
Modelling 4 (3), 408-425 (2023).
https://doi.org/10.3390/modelling4030024
• Loll, R.; Nordhausen, L.; Bieberle, A.; Schubert, M.; Pyka, T.; Koop, J.; Held,
C.; Schembecker, G.
Analysis of flow patterns in structured zickzack packings for rotating
packed beds using γ-ray computed tomography.
Ind. Eng. Chem. Res. 62 (38), 15625-15634 (2023).
https://doi.org/10.1021/acs.iecr.3c02252
• Schlüter, S.; Huxoll, F.; Grenningloh, K.; Sadowski, G.; Petzold, M.; Böhm,
L.; Kraume, M.; Skiborowski, M.
Unraveling the influence of dissolved gases on permeate flux in
organic solvent nanofiltration – Experimental analysis.
Separation and Purification Technology 295, 121265 (2022).
https://doi.org/10.1016/j.seppur.2022.121265
• Pyka, T.
Characterization of the Operating Limits of a Two-Rotor Rotating
Packed Bed.
Conference proceeding The 12th international conference Distillation &
Absorption (2022)
https://doi.org/10.1016/j.cherd.2022.10.005
• Koop, J.; Bera, N.; Quickert, E.; Schmitt, M.; Schlüter, M.; Held, C.;
Schembecker, G.
Separation of Volatile Organic Compounds from Viscous Liquids with
RPB Technology.
Ind. Eng. Chem. Res. 62 (34), 13637-13645 (2023).
https://doi.org/10.1021/acs.iecr.3c01597
• Pyka, T.; Koop, J.; Held, C.; Schembecker, G.
Dry Pressure Drop in Two-Rotor Rotating Packed Bed.
Ind. Eng. Chem. Res. 61, 17156–17165 (2022).
https://doi.org/10.1021/acs.iecr.2c02500
• Pyka, T.; Ressemann, A.; Held, C.; Schembecker, G.; Repke, J. U.
Impact of vapor bypasses on separation performance of rotating
packed beds in distillation.
Ind. Eng. Chem. Res. 62 (33), 13274-13279 (2023).
https://doi.org/10.1021/acs.iecr.3c01947
• Loll, R.; Runge, L.; Koop, L.; Held, C.; Schembecker, G.
Zickzack Packings for Deaeration in Rotating Packed Beds ─
Improved Rotor Design to Counter Bypass Flows.
Ind. Eng. Chem. Res. 61, 11934−11946 (2022).
https://doi.org/10.1021/acs.iecr.2c01443
• Hubach, T.; Schlüter, S.; Held, C.
Model-Based Optimization of Multi-Stage Nanofiltration Using the
Solution-Diffusion–Electromigration Model.
Processes 11 (8), 2355 (2023).
https://doi.org/10.3390/pr11082355
• Ascani, M.; Held, C.
Thermodynamics for reactive separations.
Book Chapter in "Process Intensification by By Reactive and
Membrane-assisted Separations" by Skiborowski and Górak
Berlin, Boston: De Gruyter (2022).
https://doi.org/10.1515/9783110720464
• Pyka, T.; Brunert, M.; Koop, J.; Bieberle, A.; Held, C.; Schembecker, G.
Novel Liquid Distributor Concept for Rotating Packed Beds.
Ind. Eng. Chem. Res. 62 (14), 5984-5994 (2023).
https://doi.org/10.1021/acs.iecr.3c00248
• Kruber, K. F.; Kroll, M.; Held, C.; Skiborowski, M.
Evaluation of the potential of a deep eutectic solvent for liquid-liquid
extraction of furfural using optimization-based process design.
Computer Aided Chemical Engineering 52, 955-960 (2023).
https://doi.org/10.1016/B978-0-443-15274-0.50152-9
• Schlüter, M.; Bhutani, S.; Bahr, J.; Wohlgemuth, K. Held, C.
Measurement and PC-SAFT Modeling of the Solubility of the BHET
Monomer, the BHET Dimer, and PET in Single Solvents.
Journal of Chemical & Engineering Data (2023).
https://doi.org/10.1021/acs.jced.3c00627
• Zawadzki, D.; Blatkiewicz, M.; Jaskulski, M.; Piątkowski, M.; Koop, J.; Loll,
R.; Górak, A.
Design and Optimisation of Structural Packings for Rotating Bed
Absorbers Using Computational Fluid Dynamics Simulation.
Chemical Engineering Research and Design 195, 508-525 (2023).
http://dx.doi.org/10.2139/ssrn.4222640
• Schlüter, S.; Franke, P.
OSN-assisted reaction and separation processes.
Book Chapter in "Process Intensification by By Reactive and
Membrane-assisted Separations" by Skiborowski and Górak
Berlin, Boston: De Gruyter (2022).
https://doi.org/10.1515/9783110720464
• Holtbrügge, J.; Pela, J. P.
Pervaporation and vapor permeation– assisted reactive separation
processes.
Book Chapter in "Process Intensification by By Reactive and
Membrane-assisted Separations" by Skiborowski and Górak
Berlin, Boston: De Gruyter (2022).
https://doi.org/10.1515/9783110720464
• Pyka, T.; Koop, J.
Rotating packed beds in distillation: rotor configurations.
Book Chapter in "Process Intensification by By Rotating Packed Beds"
by Skiborowski and Górak
Berlin, Boston: De Gruyter (2022).
https://doi.org/10.1515/9783110720464
• Loll, R.; Koop, J.
3D printed packings for rotating packed beds.
Book Chapter in "Process Intensification by By Rotating Packed Beds"
by Skiborowski and Górak
Berlin, Boston: De Gruyter (2022).
https://doi.org/10.1515/9783110720464
SCIENTIFIC HIGHLIGHTS 2023
2021
• Vondran, J.; Pela, J.; Palczewski, D.; Skiborowski, M.; Seidensticker, T.
Curse and Blessing−The Role of Water in the Homogeneously
Ru-Catalyzed Epoxidation of Technical Grade Methyl Oleate.
ACS Sustainable Chem. Eng., 34, 11469 (2021).
https://doi.org/10.1021/acssuschemeng.1c03573
• Schlüter, S.; Künnemann, K.; Freis, M.; Roth, T.; Vogt, D.; Dreimann, J.;
Skiborowski, M.
Continuous co-product separation by organic solvent nanofiltration
for the hydroaminomethylation in a thermomorphic multiphase
system.
Chem. Eng. Journal 409, 128219 (2021).
https://doi.org/10.1016/j.cej.2020.128219
• Huxoll, F.; Schlüter, S.; Budde, R.; Skiborowski, M.; Petzold, M.; Böhm, L.;
Kraume, M.; Sadowski, G.
Phase Equilibria for the Hydroaminomethylation of 1-Decene.
Journal of Chem. & Eng. Data, 66, 4484 (2021).
https://doi.org/10.1021/acs.jced.1c00561
• Scharzec, B; Merschhoff, D.; Henrichs, J.; Kappert, E. J.; Skiborowski, M.
Evaluation of membrane-assisted hybrid processes for the
separation of a tetrahydrofuran-methanol-water mixture.
Chem Eng Proc 167, 108545 (2021).
https://doi.org/10.1016/j.cep.2021.108545
• Kruber, K. F.; Grueters, T.; Skiborowski, M.
Advanced hybrid optimization methods for the design of complex
separation processes.
Computers & Chemical Engineering 147, 107257 (2021).
https://doi.org/10.1016/j.compchemeng.2021.107257
• Lukin, I.; Gładyszewski, K.; Skiborowski, M.; Górak, A.; Schembecker, G.
Aroma absorption in a rotating packed bed with a tailor-made
archimedean spiral packing.
Chemical Engineering Science 231, 116334 (2021).
https://doi.org/10.1016/j.ces.2020.116334
• Gładyszewski, K.; Groß, K.; Bieberle, A.; Schubert, M.; Hild, M.; Górak,
A.; Skiborowski, M.
Evaluation of performance improvements through application of
anisotropic foam packings in rotating packed beds.
Chemical Engineering Science 230, 116176 (2021).
https://doi.org/10.1016/j.ces.2020.116176
• Scharzec, B.; Kruber, K. F.; Skiborowski, M.
Model-based evaluation of a membrane-assisted hybrid extractiondistillation process for energy and cost-efficient purification of
diluted aqueous streams.
Chem Eng Sci, 116650 (2021).
https://doi.org/10.1016/j.ces.2021.116650
Page 59
SCIENTIFIC HIGHLIGHTS 2023
Process Automation Systems (PAS)
Page 60
SCIENTIFIC HIGHLIGHTS 2023
Page 61
Improving the control performance of a model predictive controller with
reinforcement learning for chemical processes
Dean Brandner, Torben Talis, Erik Esche, Jens-Uwe Repke, Sergio Lucia
Model predictive control (MPC) is an advanced control scheme that can optimally control nonlinear systems with multiple
inputs under consideration of constraints. However, it requires the online solution of an optimal control problem, which can
render the application intractable for real-world scenarios as it is time consuming. To solve this issue, simpler models can be
used in the optimal control problem at the expense of model accuracy leading to a worse control performance. In this work,
we apply reinforcement learning ideas to an MPC that uses a simple surrogate model based on data to recover the optimal
control performance which would be achieved when using a rigorous complex system model. We show that the trained MPC
outperforms the untrained MPC with respect to closed loop cost, and achieves a similar performance than a benchmark
MPC that uses the rigorous system model while having a significantly smaller computational cost.
Model predictive control (MPC) is a widely adopted control
scheme as it can deal with nonlinear systems with multiple inputs and constraints. However, for its application, an
optimal control problem must be solved at each sampling
time, which can be time consuming, rendering the application of MPC to a real-world system intractable. Instead of
using a full rigorous model, simpler potentially data-driven
surrogate models can be used to simplify the obtained optimization problem. Although being faster, this may cause
a worse control performance due to the less accurate system model.
Recent results in machine learning show that ideas from
reinforcement learning can be used to train an optimized
controller (also known as agent). Without having to rely
on an accurate system model in the solution process of
an optimal control problem, the agent learns the optimal
control inputs by direct interaction with the real system or
a high-fidelity simulation. For most classical cases, these
agents are neural networks. However, due to their lack
of structure, and due to the inherent nature of most reinforcement learning algorithms, the training often turns
out to be extremely data inefficient, which can be prohibitive if simulations are expensive as well.
We propose to combine methods from reinforcement
learning and optimal control and consider an MPC as
the agent instead of neural networks. In contrast to neural networks, MPC typically provides a good initial policy,
which may lie close to an optimal policy. As a result, it is
likely that less data is needed in the training process. Simultaneously, the structure of an optimization problem
allows rigorous consideration of constraints, which is not
the case for neural networks.
We investigate Q-learning as a reinforcement learning algorithm to train a MPC for a setpoint tracking example applied to a flash separation unit. Firstly, data is generated
to train neural network as a data-driven surrogate model,
which is used inside the MPC. This MPC is then trained
Contacts:
dean.brandner@tu-dortmund.de
sergio.lucia@tu-dortmund.de
using Q-learning by adapting the weights of the terminal
cost inside the MPC’s objective function. The trained controller is compared with its untrained counterpart and a
benchmark MPC, which uses the rigorous model instead
of the surrogate model. All controllers are compared with
respect to its closed-loop cost and the computation time.
Figure 1 shows the state and input trajectories (left and
right respectively) when using the mentioned controllers.
It is shown that Q-learning updates the MPC such that the
initially deviating control policy converges to the benchmark policy especially when approaching the steady state.
This also results in lower closed loop cost. Additionally, the
computation time decreases from 0.414±0.081 s (benchmark) to 0.015±0.003 s (trained).
Figure 1: Comparison of the control performance of the benchmark, untrained and
trained MPC. The dotted lines are the setpoints.
To summarize, we showed that training an MPC with
Q-learning can be used to improve an inaccurate MPC
controller and approaching the benchmark controller,
while reducing the computation time by more than an order of magnitude.
Publication:
Brandner, D.; Talis, T.; Esche, E.; Repke, J.U.; Lucia, S.,
Reinforcement learning combined with model predictive control
to optimally operate a flash separation unit. 33rd European
Symposium on Computer Aided Process Engineering, 2023, 52,
595-600.
https://doi.org/10.1016/B978-0-443-15274-0.50094-9
SCIENTIFIC HIGHLIGHTS 2023
Page 62
Sobolev Training for Data-efficient Approximate Nonlinear MPC
Lukas Lüken, Dean Brandner, Sergio Lucia
Model predictive control (MPC) is a powerful method for control of complex systems. It allows the explicit consideration of
constraints, nonlinear dynamics or economic objective functions and is also suitable for systems with multiple input and
output variables, which makes it especially interesting for process control. However, since the application of MPC requires
the solution of a nonlinear optimization problem (NLP), the real-time capability of this method poses a considerable
challenge. One possible approach to solve this problem is to leverage deep learning to approximate the control law based
on offline sampled data. This can significantly reduce the online evaluation time. To improve the data efficiency of this
learning algorithm, we combine the so-called Sobolev training with the parametric NLP sensitivities, i.e. the changes of the
optimal solution with respect to the problems parameters.
The real-time capability of MPC poses a challenge due
to the need for solving nonlinear optimization problems
(NLP) in real-time. To circumvent this problem, the control
law can be approximated using general function approximators such as neural networks. In an offline phase, the
NLP is solved for different initial states to gather data, with
which a neural network can be trained. In the online application of this approximate MPC, only one neural network
then needs to be evaluated, which can be carried out very
quickly even on limited hardware. While this approach is
able to reduce the computation time by up to multiple orders of magnitude, approximation errors can significantly
affect the performance of the controller. Therefore, a precise approximation is necessary, which, however, requires
a sufficient amount of training data. Obtaining such data
for complex systems can be challenging, even in the offline
phase, motivating an efficient use of the data.
To this end, we propose to combine the so-called Sobolev
training of neural networks with parametric sensitivities of
the underlying NLP of the MPC, to increase data efficiency
and achieve a higher approximation accuracy with the
same amount of data. The parametric sensitivities describe the local derivative of the full solution of the NLP
with respect to its parameters, including the initial states.
This information is obtained in the offline phase at negligible cost by applying the implicit function theorem to the
first-order optimality conditions (KKT conditions). Sobolev
training for neural networks involves a cost function that
reduces the deviation of the derivative of the output of the
approximate MPC from the corresponding parametric
sensitivities with respect to the initial states in addition to
the classical regression of the predicted control actions
with respect to the data:
Contacts:
lukas.lueken@tu-dortmund.de
dean.brandner@tu-dortmund.de
sergio.lucia@tu-dortmund.de
Publications:
Dean Brandner, and Sergio Lucia. "Sobolev Training for Dataefficient Approximate Nonlinear MPC." IFAC-PapersOnLine 56.2
(2023): 5765-5772
To illustrate this approach, a simulation study of an MPC
for a nonlinear continuous stirred tank reactor is presented. The results indicate that Sobolev training with the
parametric sensitivities can significantly improve the approximation accuracy of the approximate MPC, especially
with a limited amount of training data.
Furthermore, the proposed approach also provides higher
degrees of accuracy compared to other methods. Figure 1
shows the approximation accuracy for a different number
of data points used for training. Our proposed method
(Sobolev) obtains a better approximation for the same
number of data points in all cases when compared to a
standard training (nominal) or other state of the art data
augmentation techniques. Thus, by combining Sobolev
training and parametric sensitivities, an effective utilization of the available data is achieved, leading to an improved performance of the approximate MPC and enabling the use of approximate MPC for larger problems.
Figure 1: Comparison of Sobolev training with sensitivity-based data augmentation
and nominal neural network for approximate MPC of the CSTR. The figure shows
the mean absolute prediction error over the different training data sets of
increasing size.
SCIENTIFIC HIGHLIGHTS 2023
Page 63
Publications
2023
2022
Peer-reviewed Journal Articles
Peer-reviewed Journal Papers
• Brandner, D., Esche, E., Lucia, S., Renke, JU., Talis, T.
Reinforcement learning combined with model predictive control to
optimally operate a flash separation unit
Computer Aided Chemical Engineering Volume 52, 595-600 (2023)
https://doi.org/10.1016/B978-0-443-15274-0.50094-9
• Barz, T., Cruz Bournazou, MN., Groß, S., Huber, MC., Kim, JW., Krausch, N.,
Lucia, S., Neubauer, P., Schiller, SM.
High-throughput screening of optimal process conditions using
model predictive control
Biotechnology and Bioengineering Volume 119, Issue 12, 3584-3595 (2022)
https://doi.org/10.1002/bit.28236
• Fiedler, F., Lucia, S.
Improved uncertainty quantification for neural networks with
Bayesian last layer
IEEE Access, Volume 11, 123149 (2023)arXiv preprint arXiv:2302.10975 (2023)
https://doi.org/10.1109/ACCESS.2023.3329685
• Aizpuru, J., Barz, T., Bournazou, MNC., Kim, JW., Krausch, N., Lucia, S.,
Neubauer, P.
Model predictive control and moving horizon estimation for adaptive
optimal bolus feeding in high-throughput cultivation of E. coli
Computers & Chemical Engineering Volume 172, 108158 (2023)
https://doi.org/10.1016/j.compchemeng.2023.108158
• Alamo, T., Carnerero, AD., Lucia, S., Ramirez DR.
Prediction regions based on dissimilarity functions
ISA transactions, Volume 139, 49-59 (2023)
https://doi.org/10.1016/j.isatra.2023.03.048
• Castelletti, A., Cominola, A., De Schutter, B., Ficchì, A., Giuliani, M., Lucia,
S., Maestre, JM., Ocampo-Martinez, C., Segovia, P.
Model Predictive Control of water resources systems: A review and
research agenda
Annual Reviews in Control, Volume 55, 442-465 (2023)
https://doi.org/10.1016/j.arcontrol.2023.03.013
• Fiedler, F., Lucia, S.
Probabilistic multi-step identification with implicit state estimation
for stochastic MPC
IEEE Access (2023) Volume 11, 117018
https://doi.org/10.1109/ACCESS.2023.3326344
• Brabender, F., Brandner, D., Fiedler, F., Heinlein, M., Karg, B., Lucia, S.,
Lüken, L.
do-mpc: Towards FAIR nonlinear and robust model predictive control
Control Engineering Practice Volume 140, 105676 (2023)
https://doi.org/10.1016/j.conengprac.2023.105676
• Engell, S., Lucia, S., Ozkan, DM.
Optimal Facility Location and Sizing for Waste Upcycling Systems
Chemical Engineering Transactions Volume 105, 325-330 (2023)
https://doi.org/10.3303/CET23105055
Peer-reviewed Conference Papers
• Brandner, D., Lucia, S., Lüken, L.
Sobolev Training for Data-efficient Approximate Nonlinear MPC
IFAC-PapersOnLine Volume 56 Issue (2), 5765-5772 (2023)
https://doi.org/10.1016/j.ifacol.2023.10.545
• Adamek, J., Lucia, S.
Approximate Model Predictive Control Based on Neural Networks in a
Cloud-Based Environment
2023 9th International Conference on Control, Decision and Information
Technologies (CoDIT),567-572 (2023)
https://doi.org/10.1109/CoDIT58514.2023.10284471
• Döpmann, C., Fiedler, F., Lucia, S., Tschorsch, F.
Optimization-Based Predictive Congestion Control for the Tor
Network: Opportunities and Challenges
ACM Transactions on Internet Technology 22 (4), 1-30 (2022)
https://doi.org/10.1145/3520440
• Harasic, M., Kovatsch, M., Lucia, S., Mattern, D., Mazza, F., Paschke, A., Xu, J.
A Review on AI for Smart Manufacturing: Deep Learning Challenges
and Solutions
Applied Sciences, Volume 12, Issue 16, 8239 (2022)
https://doi.org/10.3390/app12168239
• Albrecht, S., Braun, S., Lucia,
Adaptively robust nonlinear model predictive control based on attack
identification
at-Automatisierungstechnik, Volume 70, Issue 4, 367-377 (2022)
https://doi.org/10.1515/auto-2021-0109
• Lucia, S., Paulen, R., Sand, G.
Special issue in honor of Sebastian Engell
Computers & Chemical Engineering, Volume 160, 107743 (2022)
https://doi.org/10.1016/j.compchemeng.2022.107743
• Braatz, RD., Findeisen, R., Lucia, S., Shen, DE., Wan, Y.
A Polynomial Chaos Approach to Robust Static Output-Feedback
Control With Bounded Truncation Error
IEEE Transactions on Automatic Control, Volume 68, Issue 1, 470-477 (2022)
https://doi.org/10.1109/TAC.2022.3140275
Peer-reviewed Conference Papers
• Karg, B., Lucia, S.
Guaranteed safe control of systems with parametric uncertainties via
neural network controllers
2022 IEEE 61st Conference on Decision and Control (CDC), 7302-7308
(2022)
https://doi.org/10.1109/CDC51059.2022.9992923
• Heinlein, M., Lucia, S., Molnar, M., Subramanian, S.
Robust MPC approaches for monotone systems*
2022 IEEE 61st Conference on Decision and Control (CDC), 2354-2360
(2022)
https://doi.org/10.1109/CDC51059.2022.9992502
• Karg, B., Lucia, S., Meske, C., Utama, C.
Explainable artificial intelligence for deep learning-based model
predictive controllers
2022 26th International Conference on System Theory, Control and
Computing (ICSTCC), 464-471 (2022)
https://doi.org/10.1109/ICSTCC55426.2022.9931794
SCIENTIFIC HIGHLIGHTS 2023
• Fiedler, F., Lucia, S.
Model predictive control with neural network system model and
Bayesian last layer trust regions
2022 IEEE 17th International Conference on Control & Automation (ICCA),
141-147 (2022)
https://doi.org/10.1109/ICCA54724.2022.9831975
• Fiedler, F., Guillén, P., Lucía, O., Lucía, S., Sarnago, H.
Deep Learning Implementation of Model Predictive Control for
Multioutput Resonant Converters
IEEE Access Volume 10, 65228-65237 (2022)
https://doi.org/10.1109/ACCESS.2022.3183746
Page 64
2021
Proceedings & Book Chapters
• Karg, B., Lucia, S.
Approximate moving horizon estimation and robust nonlinear model
predictive control via deep learning
Computers & Chemical Engineering, Volume 148, 107266 (2021)
https://doi.org/10.1016/j.compchemeng.2021.107266
• Albrecht, S., Braun, S., Lucia, S.
Attack Identification for Nonlinear Systems Based on Sparse
Optimization
IEEE Transactions on Automatic Control, Volume 67, Issue 12 (2021)
https://doi.org/10.1109/TAC.2021.3131433
• Engell, S., Lucia, S., Paulen, R., Subramanian, S.
Tube-enhanced multi-stage model predictive control for flexible
robust control of constrained linear systems with additive and
parametric uncertainties
International Journal of Robust and Nonlinear Control, Volume 31, Issue
9, 4458-4487 (2021)
https://doi.org/10.1002/rnc.5486
• Abdelsalam, Y., Engell, S., Lucia, S., Subramanian, S.
Robust Tube-Enhanced Multi-Stage NMPC With Stability Guarantees
IEEE Control Systems Letters Volume 6, 1112-1117 (2021)
https://doi.org/10.1109/LCSYS.2021.3089502
• Alamo, T., Karg, B., Lucia, S.
Probabilistic performance validation of deep learning-based robust
NMPC controllers
International Journal of Robust and Nonlinear Control, Volume 31, Issue
18, 8855-8876 (2021)
https://doi.org/10.1002/rnc.5696
• Braatz, RD., Findeisen, R., Lucia, S., Shen, DE., Wan, Y.
Polynomial chaos-based H2 output-feedback control of systems with
probabilistic parametric uncertainties
Automatica, Volume 131, 109743 (2021)
https://doi.org/10.1016/j.automatica.2021.109743
• Karg, B., Lucia, S.
Model Predictive Control for the Internet of Things
Recent Advances in Model Predictive Control, 165-189 (2021)
https://doi.org/10.1007/978-3-030-63281-6_7
Peer-reviewed Conference Papers
• Darup, MS., Faulwasser, T., Lucia, S., Mönnigmann, M.
Teaching MPC: Which Way to the Promised Land?
IFAC-PapersOnLine, Volume 54, Issue 6, 238-243 (2021)
https://doi.org/10.1016/j.ifacol.2021.08.551
• Lucia, S., Yang, Y.
Multi-step Greedy Reinforcement Learning Based on Model
Predictive Control
IFAC-PapersOnLine, Volume 54, Issue 3, 699-705 (2021) (Keynote paper)
https://doi.org/10.1016/j.ifacol.2021.08.323
• Karg, B., Lucia, S.
Reinforced approximate robust nonlinear model predictive control
23rd International Conference on Process Control, 149-156 (2021) (Best
Paper by Young Author Award)
https://doi.org/10.1109/PC52310.2021.9447448
SCIENTIFIC HIGHLIGHTS 2023
• Fiedler, F., Lucia, S.
On the relationship between data-enabled predictive control and
subspace predictive control
European Control Conference (ECC), 222-229 (2021)
https://doi.org/10.23919/ECC54610.2021.9654975
• Kovatsch, M. Lucia, S., Xu, J.
Open Set Recognition for Machinery Fault Diagnosis
IEEE 19th International Conference on Industrial Informatics (INDIN),
1-7 (2021)
https://doi.org/10.1109/INDIN45523.2021.9557572
• Döpmann, C., Fiedler, F., Lucia, S., Tschorsch, F.
Towards Optimization-Based Predictive Congestion Control for the
Tor Network
Electronic Communications of the EASST, Volume 80 (2021)
http://dx.doi.org/10.14279/tuj.eceasst.80.1128
• Bermbach, D., Handziski, V., Lucia, S., Wolisz, A.
Towards grassroots peering at the edge
Proc. of the 8th International Workshop on Middleware and Applications
for the Internet of Things, 14-17 (2021)
https://doi.org/10.1145/3493369.3493602
Page 65
SCIENTIFIC HIGHLIGHTS 2023
Reaction Engineering and Catalysis (REC)
Page 66
SCIENTIFIC HIGHLIGHTS 2023
Page 67
Flow characterization of additively manufacturable periodic open cellular
structures in the context of heterogeneous catalysis
Diamond unit cell-based interpenetrating periodic open cellular structures
Sebastian Trunk, Lisa Eckendörfer, Andreas Brix, Hannsjörg Freund
Additively manufactured lattice-like catalyst support structures, known as Periodic Open Cellular Structures (POCS),
serve as an innovative alternative to traditional randomly packed beds of catalyst pellets in heterogeneous catalysis.
The conventional packed bed technology suffers from high pressure drop and inefficient radial heat transfer due to
minimal contact points among the pellets. In contrast, POCS offer a continuous solid matrix as well as substantial voids.
This design ensures efficient radial heat and mass transfer, along with reduced pressure drop. The adaptability inherent
to additive manufacturing allows for the precise tailoring of these structures to meet specific reactor requirements of
a chemical process. However, to fine-tune and optimize the design and its performance, a thorough understanding is
essential. High potential is attributed to interPOCS, a subset of POCS, with the ability to in-operando adjust the position
of a second interwoven structure.
The periodic unit cell formed by characteristically arranged solid struts is the basis of POCS. The POCS lattice
is created by repeating the underlying unit cell, e.g. the diamond unit cell, in all three spatial directions. In interpenetrating POCS (interPOCS), two of these lattices are interwoven in such a way that a relative displacement of the
two independently movable structures is possible. The
offset of the interPOCS is a quantitative measure of the
relative shift. It is defined as the ratio of the distance between the two structures and the unit cell size as a measure of the maximum distance (see Fig. 1). For a shift of
50%, one structure is placed exactly in the center of the
other. As one structure is moved further away from the
other, the value of the offset increases.
The local flow field is strongly influenced by the offset. The
flow path evolves from a double helix to a single helix like
flow with increasing offset (Fig. 2). As a result, the mean
tortuosity and especially the frequency distribution of the
tortuosity can be adjusted in-operando via the offset (Fig.
3). This illustrates the high potential of interPOCS to alter
relevant transport properties in chemical reactors in-operando. This feature is particularly expected to enable dynamic reactor operation playing an increasingly important
role, e.g., in modern Power-to-X processes.
Figure 2: Helix shaped flow path through an interPOCS channel for an offset of
50% (double helix) and 75% (single helix).
Figure 1: Schematic visualization of the diamond unit cell (left) and the calculation
of the offset (right) for an interPOCS with fixed structure in grey and moveable
structure in red.
We investigated the pressure drop and flow field characteristics of interPOCS as function of the offset position
using computational fluid dynamics (CFD) simulations and
our in-house particle tracking tool. Based on this detailed
analysis, the pressure drop results of µCT-based digital duplicates show good agreement with previous experiments
on 3D printed interPOCS and a notable dependence of the
pressure drop on the offset position could be confirmed.
Contact:
lisa.eckendoerfer @tu-dortmund.de
andreas.brix@tu-dortmund.de
hannsjoerg.freund@tu-dortmund.de
Figure 3: Normalized frequency distribution of the tortuosity for various offsets.
Publications:
Trunk, S.; Freund, H., Chem. Eng. Process. Process Intensif. 2024,
195, 109617. https://doi.org/10.1016/j.cep.2023.109617.
Ferroni, C.; Bracconi M.; Ambrosetti M.; Groppi G.; Maestri M.;
Freund, H.; Tronconi E., Chem. Eng. Process. Process Intensif. 2024,
195, 109613. https://doi.org/10.1016/j.cep.2023.109613.
SCIENTIFIC HIGHLIGHTS 2023
Page 68
Dynamically Operated Fixed Bed Reactors for CO2 Methanation
Strategies to Mitigate Catalyst Deactivation
David Kellermann, Moritz Langer, Hannsjörg Freund
Due to the fluctuating power generation from renewable sources, reactors within the power-to-X process concepts such as,
e.g., the CO2 methanation are confronted with partly strongly fluctuating feed flows. Dynamic reactor operation, however,
can lead to temporally critical hot spots or unfavorable gas phase conditions, which increase the deactivation rate of
the catalyst and shortens its lifetime. To investigate these effects we developed a kinetic model for the methanation
reaction that describes the reaction kinetics as well as the catalyst deactivation based on experiments conducted in a
gradientless Berty-type reactor. Based on these results, we are able to model and design a load-flexible industrial-scale
fixed-bed reactor and describe catalyst deactivation in dynamic operation. This in turn provides a basis for the derivation
of adapted policies for dynamic operation to extend the catalyst service life.
The transition of the energy sector from fossil fuels to renewable energies is currently of great interest to researchers. In this context, Power-to-X (PtX) technologies such as
methanation are considered to play a crucial role. The
methane produced can be easily stored, distributed, and
used as a natural gas substitute by utilizing existing natural gas infrastructure. In this scenario, hydrogen is provided on site by water electrolysis, which can follow the fluctuations of renewable energy generation comparatively
easily. However, fluctuations in the reactant supply of PtX
plants pose challenges for the operation of the catalytic
reactors, particularly because of the exothermic nature of
the methanation reaction. We developed a kinetic model
based on a Langmuir-Hinshelwood-Hougen-Watson approach for an industrial Ni on AlOX catalyst, which is capable of describing both, catalytic activity over a broad operation range as well as catalyst deactivation according to
the given conditions. For this, we used a lab-scale plant
comprising a Berty-type reactor, which allows kinetic measurements in the absence of mass and heat transfer limitations and provides gradientless reaction conditions.
The deactivation behavior was investigated by long-term
experiments of up to 120 h time on stream, varying in temperature, pressure and the volume flow to catalyst mass
ratio. We developed a reactor design optimized simultaneously for multiple steady-state operating points within a
desired load range. This leads to a high load flexibility while
ensuring the required product gas quality for all scenarios.
Using this obtained reactor design, we investigated three
different operation scenarios for a year of operation under
fluctuating inlet conditions. In case 1, inlet volume flow
and composition are constant (H2/CO2 = 4/1), in case 2, the
Publications:
D. Kellermann, M. Langer, H. Freund, Annual Meeting on Reaction
Engineering, Frankfurt, Germany (2023).
D. Kellermann, M. Langer, H. Freund, International Symposium on
Chemical Reaction Engineering, Québec, Canada (2023).
M. Langer, D. Kellermann, H. Freund, Kinetic modeling of
dynamically operated heterogeneously catalyzed reactions:
Microkinetic model reduction and semi-mechanistic approach on
the example of the CO2 methanation. Chem. Eng. J., 467, 143217,
2023. https://doi.org/10.1016/j.cej.2023.143217
flow rate is fluctuating while the composition is constant
(see Fig. 1) and in case 3, the inlet flow rate fluctuates as
well as the H2 to CO2 ratio. The simulation results show a
significantly accelerated deactivation of the catalyst at
over-stoichiometric CO2 concentrations in the feed (see
Fig. 2). Consequently, such operating conditions should be
avoided by reducing the CO2 supply at insufficient hydrogen production rates in PtX-plants.
Figure 1: Development of the temperature and the hydrogen conversion in the
reactor over the simulated time span of one year under fluctuating inlet volume
flow (case 2). An activity front moves through the reactor and results in a
significant decrease in product quality at breakthrough.
Figure 2: Comparison of the H2 conversion for all scenarios at different
dimensionless reactor lengths z. Case 1 and 2 show similar deactivation
characteristics, whereas in case 3, it is significantly accelerated because of high
CO2 feed concentrations.
Contacts:
david.kellermann@tu-dortmund.de
hannsjoerg.freund@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 69
Process Intensification of Gas-Liquid Reactors
Identification of Mass Transfer Limitations by Kinetic Modeling of a Large-Scale Trickle Bed Reactor for
Viscous Aromatics Hydrogenation
Hendrik Held, Hannsjörg Freund
Trickle bed reactors (TBRs) play a pivotal role in the refinement of over 1.6 gigatons of chemical products annually,
establishing them as the predominant reactor type for heterogeneously catalyzed reactions involving liquids and dissolved
gases. Common fields of application are hydrodesulfurization, hydrogenation, and oxidation reactions. TBRs face
challenges related to mass transfer due to the low gas solubility and slow diffusion in the liquid phase. The significance of
mass transfer in TBRs needs to be considered in catalyst selection and reactor design, as inadequate supply of reactants
to the catalyst may lead to diminished reaction rates and increased side product formation. Addressing these mass
transfer challenges is crucial for process intensification of TBRs in various chemical processes.
We developed a reactor model for elucidating the interplay between mass transfer and reaction kinetics within
TBRs based on extensive experimental data. The hydrogenation of high-molecular weight aromatics under high
pressure (7-9 MPa) and moderate temperature (90-120 °C)
was chosen as model reaction system. An industrial-standard egg-shell catalyst was used for the investigations
and compared to reference catalyst systems. A miniplantscale trickle bed loop reactor (TBLR) was designed enabling the measurement of a packed bed system free of
external mass transfer influences. It was proven that the
TBLR operates as a differential reactor with a per pass
conversion below 2%, enabling the calculation as an ideally backmixed differential reactor due to the high external
recycle flow rate. Analytical techniques, including GC-FID,
UV−Vis, and NMR, were employed for thorough analysis.
This combination allows for precise examination of aromatic concentration within a mixture containing isomeric
species.
moderate affinity for adsorption at active sites. The developed Plug Flow Reactor (PFR) model, incorporating a discretized pore diffusion model (1D + 1D), see Fig. 1, and a neural network approach for mass transfer estimation, provides
detailed insights into concentration profiles within the reactor, encompassing the catalyst pore network. The method identified hydrogen pore diffusion limitations for an industrial-standard catalyst under process conditions, even
with the use of an eggshell catalyst featuring a 200 μm shell
(Fig. 2). The average pore effectiveness was estimated to 1124 % within the specified operation range.
Figure 2: Concentration profiles for g-, l- and s-phase for a fixed bed length of 0.75
m. Green: educt, orange: product, black: H2, solid line: T = 90 °C, dash-dotted line:
T = 120 °C.
Figure 1: 1D + 1D domain for kinetic modeling of a trickle bed reactor.
The study introduces a simplified method for estimating
the activation energy. Utilizing the kinetic Langmuir-Hinshelwood-Hougen-Watson (LHHW) approach, the adsorption of cyclohexane species was shown to not significantly
impact the reaction rate, whereas aromatic species e
xhibit
Contacts:
hannsjoerg.freund@tu-dortmund.de
In contrast to reaction systems with components of low
molecular mass, where gas-liquid mass transfer is typically the primary resistance, differing mass transfer relations
were observed for the investigated viscous component
system with slow hydrogenation rates. The presented
findings advance the understanding of mass transfer phenomena in complex gas-liquid systems, particularly those
involving high-viscosity components undergoing hydrogenation. The developed model enables identification of
mass transfer limitations in TBRs, thereby establishing the
foundation for effective process intensification.
Publications:
Held, H., Freund, H., Identification of Mass Transfer Limitations by
Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the
Hydrogenation of Viscous Aromatics. Ind. Eng. Chem. Res. 2024, 63
(1), 147-162. https://doi.org/10.1021/acs.iecr.3c03273
SCIENTIFIC HIGHLIGHTS 2023
Page 70
Publications
2023
2022
Journal Articles (with peer review)
Journal Articles (with peer review)
• Engl, T.; Langer, M.; Freund, H.; Rubin, M.; Dittmeyer, R.
Tap Reactor for Temporally and Spatially Resolved Analysis of the
CO2 Methanation Reaction
Chem.-Ing.-Tech. 95(5), 658-667 (2023)
https://doi.org/10.1002/cite.202200204
• Wehinger, G. D.; Ambrosetti, M.; Cheula, R.; Ding, Z.; Isoz, M.; Kreitz, B.;
Kuhlmann, K.; Kutscherauer, M.; Niyogi, K.; Poissonnier, J.; Réocreux, R.;
Rudolf, D.; Wagner, J.; Zimmermann, R.; Bracconi, M.; Freund, H.; Krewer,
U.; Maestri, M.
Quo Vadis Multiscale Modeling in Reaction Engineering? – A Perspective
Chemical Engineering Research and Design, 184, 39-58 (2022)
https://doi.org/10.1016/j.cherd.2022.05.030
• Freund, H.; Sauer, J.; Wachsen, O.
„Digitalisierung der Reaktionstechnik“: Ein Themenfeld mit vielen
Facetten!
Editorial, Chem.-Ing.-Tech. 95(5), 619 (2023)
https://doi.org/10.1002/cite.202370502
• Langer, M.; Kellermann, D.; Freund, H.
Kinetic modeling of dynamically operated heterogeneously catalyzed
reactions: Microkinetic model reduction and semi-mechanistisc
approach on the example of the CO2 methanation
Chemical Engineering Journal 467, 143217 (2023)
https://doi.org/10.1016/j.cej.2023.143217
• Ferroni, C.; Bracconi, M.; Ambrosetti, M.; Groppi, G.; Maestri, M.; Freund,
H.; Tronconi, E.
Process Intensification in Mass-Transfer Limited Catalytic Reactors
Through Anisotropic Periodic Open Cellular Structures
Chem. Eng. Process. 195, 109613 (2024)
• Worgul, B.; Aguilera, A. F.; Vergat-Lemercier, C.; Eränen, K.; Simakova, O.;
Held, H.; Freund, H.; Murzin, D. Y.; Salmi, T.
Sugar Acid Production on Gold Nanoparticles in Slurry Reactor:
Kinetics, Solubility and Modelling
Chemical Engineering Science 260, 117948 (2022)
https://doi.org/10.1016/j.ces.2022.117948
• Freund, H.; Sauer, J.; Wachsen, O.
Wie verändert sich die Reaktions- und Reaktortechnik durch die
Elektrifizierung chemischer Prozesse?
Editorial, Chemie Ingenieur Technik 94(5), 615 (2022)
https://doi.org/10.1002/cite.202270502
SCIENTIFIC HIGHLIGHTS 2023
2021
Journal Articles (with peer review)
• Fischer, K. L.; Freund, H.
Intensification of Load Flexible Fixed Bed Reactors by Optimal Design
of Staged Reactor Setups
Chemical Engineering and Processing 159, 108183 (2021)
https://doi.org/10.1016/j.cep.2020.108183
• Littwin, G.; Röder, S.; Freund, H.
Systematic Experimental Investigations and Modeling of the
Heat Transfer in Additively Manufactured Periodic Open Cellular
Structures with Diamond Unit Cell
Industrial & Engineering Chemistry Research, 60(18), 6753-6766 (2021)
https://doi.org/10.1021/acs.iecr.0c06210
• Moioli, E.; Schmid, L.; Wasserscheid, P.; Freund, H.
Kinetic Modelling of Reactions for the Synthesis of 2-Methyl-5-EthylPyridine
Reaction Chemistry & Engineering, 6, 1254-1264 (2021)
https://doi.org/10.1039/D1RE00085C
• Trunk, S.; Brix, A.; Freund, H.
Development and Evaluation of a New Particle Tracking Solver for
Hydrodynamic and Mass Transport Characterization of Porous Media
– A Case Study on Periodic Open Cellular Structures
Chemical Engineering Science 244, 116768 (2021)
https://doi.org/10.1016/j.ces.2021.116768
• Littwin, G.; von Beyer, M.; Freund, H.
Detailed Investigation of Liquid Distribution and Holdup in Periodic
Open Cellular Structures Using Computed Tomography
Chemical Engineering and Processing 168, 108579 (2021)
https://doi.org/10.1016/j.cep.2021.108579
• Freund, H.; Sauer, J.; Wachsen, O.
“Circular Economy” – ein neues und zugleich altes Arbeitsgebiet der
Reaktionstechnik
Editorial, Chemie Ingenieur Technik 93(5), 735 (2021)
https://doi.org/10.1002/cite.202170502
Page 71
SCIENTIFIC HIGHLIGHTS 2023
Technical Biochemistry (TB)
Page 72
SCIENTIFIC HIGHLIGHTS 2023
Page 73
Improving CBCA synthase activity through rational protein design
Fabian Thomas & Oliver Kayser
Global interest for the minor cannabinoid cannabichromene (CBC) is growing steadily, as potential pharmaceutical
applications continue to emerge. Due to low-yielding and unspecific extraction processes from its plant host Cannabis
sativa, a biotechnological production is desirable. The complete heterologous biosynthesis of several other cannabinoids
has recently been demonstrated as an accessible platform. However, the enzyme involved in the biosynthesis of CBC
precursor cannabichromenic acid (CBCA) suffers from comparatively low catalytic efficiency, has not been crystallized,
and remains poorly characterized.
Terpenophenolic cannabinoids are the most prominent
secondary metabolites in the annual herb Cannabis sativa
L. Rare cannabinoids received slightly less public and scientific attention, but cannabichromene (CBC-C5) as the
most abundant among them is nonetheless subject to
several clinical studies for its anti-inflammatory, immunoprotective, anti-bacterial, and anti-fungal propertie
were used by cultivating three different clones from each
integration plate. In vitro cell lysate conversion assays
were performed at enzyme optimum conditions by addition of the substrate CBGA. After protein precipitation and
centrifugation, the assay supernatant was analyzed on an
HPLC-UV system to detect the newly formed CBCA.
Figure 1: Biosynthesis of Δ9-tetrahydrocannabinolic acid (THCA) and
cannabichromenic acid (CBCA) by their respective enzymes in Cannabis sativa. In
an oxidative cyclization the common precursor cannabigerolic acid is converted
to THCA or CBCA, which can be transformed to the bioactive neutral cannabinoids
Δ9-tetrahydrocannabinol (THC-C5) or cannabichromene (CBC-C5) by heat
decarboxylation.
Figure 2: Enzyme activity of variants assessing structure-function relationships
of CBCA synthase. CBCA content detected by HPLC-UV at 255 nm after 1 h CBGA
bioconversion assays at pH 4.85, normalized to wild type enzyme content. The
analysis confirms that Y484, H114, C176 and W444 are essential residues for
CBCAS, like was shown previously for THCAS. Much different are results for
residues Y417 and H292, as well as for certain N-glycosylation sites, where CBCAS,
in contrast to THCAS, was much less affected.
Cannabinoids are produced by specialized berberine
bridge-like oxidoreductases through an oxidative cyclization of the linear isoprenoid precursor cannabigerolic acid
(CBGA-C5, Fig. 1). While THCA synthase and CBDA synthase
have been studied thoroughly since their first characterization 20 years ago, research concerning CBCA synthase
is in its infancy. The gene encoding CBCAS was identified
recently, and the CBCA activity of the corresponding protein, expressed in Komagataella phaffii, was confirmed.
For the analysis, the wild type sequence and the respective CBCAS variants were expressed from single-copy genomic integrations in Komagataella phaffii cells. For all
subsequent expression cultures biological triplicates
Contact:
oliver.kayser@tu-dortmund.de
Some variants, however, performed differently for both enzymes and thus hint towards a divergent binding mode of
the common precursor cannabigerolic acid (CBGA) within
the active site. Besides structure-function considerations,
the other aspect of this research was sophisticated enzyme engineering towards facilitated CBCA activity. For
the lysate containing variant C244W, a 22-fold increase in
CBCA activity was confirmed, far exceeding the expectations. A total of five positions within CBCAS were identified
where amino acid substitution resulted in a significant elevation of CBCA activity in cell lysates of the corresponding variants.
Publications:
Thomas, F.; Kayser, O.: Improving CBCA synthase activity through
rational protein design. J Biotechnol Feb 10:363:40-49.
doi: 10.1016/j.jbiotec.2023.01.004.
SCIENTIFIC HIGHLIGHTS 2023
Page 74
Generation of Cannabigerolic Acid Derivatives and Their Precursors by Using the
Promiscuity of the Aromatic Prenyltransferase NphB
Saskia Spitzer, Jasmin Wloka, Jörg Pietruszka, Oliver Kayser
NphB is an aromatic prenyltransferase with high promiscuity for phenolics including flavonoids, isoflavonoids, and plant
polyketides. It has been demonstrated that cannabigerolic acid is successfully formed by the reaction catalysed by NphB
using geranyl diphosphate and olivetolic acid as substrates. In this study, the substrate specificity of NphB was further
determined by using olivetolic acid derivatives as potential substrates for the formation of new synthetic cannabinoids.
The derivatives differ in the hydrocarbon chain attached to C6 of the core structure.
NphB, a protein isolated from Streptomyces sp. strain
CL190, belongs to the enzyme class of aromatic prenyltransferases and the ABBA superfamily. The natural prenyl
donor substrate is GPP, but the donor substrate specificity
depends on the acceptor substrate. The enzyme catalyzes
a C-prenylation at the ortho- or para-position of a hydroxy
group, but O-prenylation has also been observed on single
hydroxy groups of flavonoids. Because NphB, like CsPT4,
can catalyze the reaction to CBGA-C5, we extrapolated
this fact to cannabinoid production.
strates. The resorcylate core is shifted towards the
π-chamber by exchanging tyrosine at position 288 to a alanine and introducing a polar amino acid side chain with
serine at position 286. Two different hydrogen bond networks stabilize when comparing the two proteins. For the
NphB G286S/Y288A variant, a construct consisting of two
hydrogen bonds between Ser214 and OH4 and between
Ser286 and the carboxyl group was identified. For NphB
wild type, this network consists of Ser214 and the carboxyl
group, and Tyr288 and OH4 (Figure 1). A shift in the proximity between substrate and reaction partner GPP explains
the different prenylation pattern of the variant compared
to the wild type.
Figure 1: The conversion of novel olivetolic acid derivatives with the highly
promiscuous prenyltransferase NphB is analyzed as a tool for the creation of
synthetic cannabinoid libraries.
In this study, the substrate specificity of NphB is further
evaluated concerning the conversion of various olivetolic acid derivatives. Novel substrates were synthesized by
modifying the pentyl chain with different hydrocarbon
moieties. In silico experiments were performed to generate a diversified substrate library. This substrate library
was evaluated with in vitro assays regarding their conversion with NphB towards CBGA-derivatives.
The NphB wild type primarily catalyzes the formation of
2-O-GOA, and the variant G286S/Y288A predominantly
forms CBGA-C5 using olivetolic acid and GPP as subPublications:
Spitzer, S.; Wloka,J.; Pietruszka, J.; Kayser, O.
Generation of Cannabigerolic Acid Derivatives and Their
Precursors by Using the Promiscuity of the Aromatic
Prenyltransferase NphB. ChemBioChem 2023, 24 (22): e202300441
https:// doi: 10.1002/cbic.202300441
Figure 2: Hydrolysis of the PBI esters shown in Fig. 1 in different aqueous buffer
solutions. The MICS.aureus values of the partially hydrolyzed polymers were
determined and the respective values are marked as areas (alternating grey/
white) in the diagrams.
Novel compounds containing the olivetolic acid resorcylate
core and structural elements beyond the natural pentyl
group have been synthesized and evaluated as potential
substrates for NphB. Alkyl chain modifications up to an octyl group attached to the core are accepted as substrates
and show similar conversion to olivetolic acid. A further
analysis of the prenylation pattern was carried out for the
most promising molecules. In an organism, like S. cerevisiae,
NphB expression and feeding of olivetolic acid derivatives
could lead to the formation of CBGA derivatives
Contacts:
saskia.spitzer@tu-dortmund.de
oliver.kayser@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 75
Publications
2023
2021
Peer-Reviewed Journal Articles
Peer-reviewed Journal Articles
• Erin Noel Jordan, Christina Schmidt, Oliver Kayser
Foldseek reveals a CBGA prenylating enzyme GlyMa_02G168000
from Glycine max
Biochem Biophys Res Commun Feb 12:696:149471 (2024)
DOI: 10.1016/j.bbrc.2024.149471
• Tajammul Hussain, Ganga Jeena, Thanet Pitakbut, Nikolay Vasilev, Oliver
Kayser
Cannabis sativa research trends, challenges, and new-age
perspectives
iScience Nov 1;24(12):103391 (2021).
DOI: 10.1016/j.isci.2021.103391
• Saskia Spitzer, Jasmin Wloka, Jörg Pietruszka, Oliver Kayser
Generation of Cannabigerolic Acid Derivatives and Their Precursors
by Using the Promiscuity of the Aromatic Prenyltransferase NphB
Chembiochem Nov 16;24(22):e202300441 (2023)
DOI: 10.1002/cbic.202300441
• Fabian Thomas, Oliver Kayser
Improving CBCA synthase activity through rational protein design
J Biotechnol Feb 10:363:40-49 (2023)
DOI: 10.1016/j.jbiotec.2023.01.004
2022
Peer-reviewed Journal Articles
• Erin Jordan, Gia-Nam Nguyen, Alexander Piechot, Oliver Kayser
Cannabinoids as New Drug Candidates for the Treatment of
Glaucoma
Planta Med Nov;88(14):1267-1274 (2022)
DOI: 10.1055/a-1665-3100
• Thanet Pitakbut, Gia-Nam Nguyen, Oliver Kayser
Activity of THC, CBD, and CBN on Human ACE2 and SARS-CoV1/2
Main Protease to Understand Antiviral Defense Mechanism
Planta Med Oct;88(12):1047-1059 (2022)
DOI: 10.1055/a-1581-3707
• Gia-Nam Nguyen, Erin Noel Jordan, Oliver Kayser
Synthetic Strategies for Rare Cannabinoids Derived from Cannabis
sativa
J Nat Prod Jun 24;85(6):1555-1568 (2022)
DOI: 10.1021/acs.jnatprod.2c00155
• Thanet Pitakbut, Michael Spiteller, Oliver Kayser
Genome Mining and Gene Expression Reveal Maytansine Biosynthetic
Genes from Endophytic Communities Living inside Gymnosporia
heterophylla (Eckl. and Zeyh.) Loes. and the Relationship with the
Plant Biosynthetic Gene, Friedelin Synthase
Plants (Basel) Jan 25;11(3):321 (2022)
DOI: 10.3390/plants11030321
• Leonie Hillebrands, Marc Lamshoeft , Andreas Lagojda, Andreas Stork,
Oliver Kayser
In vitro metabolism of tebuconazole, flurtamone, fenhexamid,
metalaxyl-M and spirodiclofen in Cannabis sativa L. (hemp) callus
cultures
Pest Manag Sci Dec;77(12):5356-5366 (2021)
DOI: 10.1002/ps.6575
• Thanet Pitakbut , Michael Spiteller , Oliver Kayser
In Vitro Production and Exudation of 20-Hydroxymaytenin from
Gymnosporia heterophylla (Eckl. and Zeyh.) Loes. Cell Culture
Plants (Basel) Jul 21;10(8):1493 (2021)
DOI: 10.3390/plants10081493
SCIENTIFIC HIGHLIGHTS 2023
Technical Biology (TBL)
Page 76
SCIENTIFIC HIGHLIGHTS 2023
Page 77
New Antiparasitic Drugs by Whole-Cell Biotransformation
Conversion of Quinolone Precursor Molecules into Aurachin Antibiotics
Sebastian Kruth, Cindy J.-M. Zimmermann, Stephan Lütz, Jörg Pietruszka, Marcel Kaiser, Markus Nett
The natural product aurachin D is a farnesylated quinolone alkaloid, which is known to possess activity against the
causative agent of malaria, Plasmodium falciparum. Using a previously constructed Escherichia coli strain that is capable
of aurachin biosynthesis, we now generated nine structural derivatives of this antibiotic by whole-cell biotransformation.
Bioactivity testing confirmed the antimalarial properties of aurachins and further revealed some of these compounds as
extremely potent antileishmanial agent with IC50 values in the lower micromolar or even nanomolar range.
Aurachin D (1) belongs to a family of bacterial quinolone
antibiotics that are highly active against parasitic protozoa causing malaria. Previously we had described a scalable process for the biocatalytic production of 1 from the
commercially available precursor molecule 2-methyl-1Hquinolin-4-one using a recombinant E. coli strain.
Figure 1: The same strain was now used for the conversion of synthetically
prepared analogues of 2-methyl-1H-quinolin-4-one into aurachin derivatives.
The substrate analogues were produced in a two-step
sequence from ethyl acetoacetate and substituted aniline derivatives. Following their purification and structural verification, these compounds were added to growing cultures of the recombinant E. coli strain. Overall,
we observed satisfactory conversion rates and a broad
substrate tolerance. Nine out of twelve tested precursor
analogues were successfully converted into aurachin derivatives. Only substrates featuring bulky substituents on
the aromatic ring system (e.g., nitro or hexyl groups) were
not processed.
Consistent with previous literature reports, 1 showed potent antiplasmodial effects with an IC50 value of 0.012 μM
against the malaria parasite Plasmodium falciparum (Table 1). In addition, we observed significant trypanocidal
activities. The IC50 values of 1 against the causative agents
of sleeping sickness (Trypanosoma brucei rhodesiense)
and Chagas disease (Trypanosoma cruzi) were in the lower micromolar range, i.e., 4.5 μM and 1.3 μM, respectively.
In the case of Leishmania donovani, which causes visceral
leishmaniasis, 1 was even active at nanomolar concentrations (IC50 0.044 μM). The bioactivity testing revealed further that the antiprotozoal properties of aurachin D can
be significantly altered by furnishing its quinolone backbone with different functional groups. Although none of
the generated derivatives showed increased activities
against the tested protozoa in comparison to 1, the lack of
consistent structure-activity relationship trends suggests
that the aurachins exert their effects via different targets
in the tested protozoa and also in mammalian cells.
Table 1: Activities of aurachin D and the generated derivatives against parasitic protozoa and mammalian cells. IC50 values are given in μM.
The antileishmanial selectivity index (S.I) was determined as IC50 (L6)/IC50 (L. donovani).
IC50
Plasmodium
falciparum
NF54
IC50
Trypanosoma brucei
rhodesiense STIB 900
aurachin D
0.012
2-desmethyl aurachin D
0.006
Test Compound
IC50
Trypanosoma cruzi
Tulahuen C4
IC50
Leishmania donovani
MHOM-ET-67/L82
IC50
Rat
Myoblast
L6 Cells
Antileishmanial
S.I.
4.5
1.3
0.044
130.7
2969.5
9.5
2.4
1.5
20.4
13.2
4.3
6-methyl aurachin D
0.514
43.2
7.6
4.3
18.6
7-methyl aurachin D
0.007
163.8
45.7
9.1
65.3
7.2
6-methoxy aurachin D
0.866
40.3
19.3
7.3
118.3
16.2
7-methoxy aurachin D
0.089
44.8
21.9
17.1
80.8
4.7
6-fluoro aurachin D
0.061
37.2
1.8
0.617
125.8
203.9
6-chloro aurachin D
0.021
37.4
11.2
6.2
117.5
18.9
7-chloro aurachin D
0.070
104.9
41.8
9.2
54.7
5.9
6-bromo aurachin D
0.119
40.2
22.6
13.9
107.7
7.7
Contact:
markus.nett@tu-dortmund.de
Publications:
Kruth, S.; Zimmermann, C. J.-M.; Kuhr, K.; Hiller, W.; Lütz, S.;
Pietruszka, J.; Kaiser, M.; Nett, M., Generation of Aurachin
Derivatives by Whole-Cell Biotransformation and Evaluation of
Their Antiprotozoal Properties. Molecules 2023, 28, 1066. https://
doi.org/10.3390/molecules28031066.
SCIENTIFIC HIGHLIGHTS 2023
Page 78
Biocatalytic Flow Synthesis of Heterocycles
Design of an Immobilized Enzyme Reactor for the Condensing Amidohydrolase MxcM
Lea Winand, Stefanie Theisen, Stephan Lütz, Katrin Rosenthal, Markus Nett
Heterocycles are important structural elements in pharmaceuticals and agrochemicals. In 2022, 83% of the 200 topselling small molecule pharmaceuticals featured at least one heterocyclic motif. The chemical synthesis of heterocycles
typically requires harsh reaction conditions and the use of hazardous agents. Because of these deficiencies, the synthetic
utility of enzymes in heterocyclic chemistry is increasingly explored. Of particular interest in this context are condensing
amidohydrolases due to their tolerance towards organic solvents and their independence of cosubstrates. An example for
such an enzyme is the imidazoline-forming amidohydrolase MxcM, which has now been integrated into an immobilized
enzyme reactor (IMER) that can be operated under flow conditions.
In 2018, the amidohydrolase MxcM was discovered in the
marine bacterium Pseudoalteromonas piscicida. This enzyme was found to convert monoacylated 1,2-diamines
into imidazoline residues. A biochemical characterization
of MxcM revealed that this enzyme exhibits high stability
and tolerance towards organic solvents. Furthermore, it
does not require cosubstrates for its catalytic activity. For
these reasons, MxcM is a promising biocatalyst for integration into chemical process synthesis of heterocyclic
compounds. To further evaluate the synthetic utility of this
enzyme, we first developed a concept for the immobilization of MxcM. Immobilization is generally known to increase the operational stability of enzymes and makes
them re-usable. A hexahistidine tag was used for fixation
on a solid, porous carrier. Our immobilization protocol
leads to immobilization yields of ~75% and enzyme loadings between 7 and 8 wt%. In buffer, the remaining activity
of the immobilized MxcM amounted to 30–40% compared
to the free enzyme. Since immobilization can influence
the solvent tolerance of enzymes, we also analyzed the
activity of the immobilized MxcM in different solvent systems (Figure 1).
We observed that the immobilization improved the tolerance of MxcM to all tested organic solvents. Due to the
good solvent and storage stability, we further probed the
performance of immobilized MxcM for biocatalysis in flow.
For that purpose, packed bed-reactors were designed and
installed into an HPLC system (Figure 2).
Technical Biochemistry (TB)
Figure 2: Schematic representation of immobilized enzyme reactor (MxcM-IMER)
used for biocatalytic flow synthesis of imidazoline heterocycles.
Interestingly, the composition of the mobile phase greatly
influenced the conversion, while the residence time and the
temperature had only minor impact under the tested conditions. The MxcM-IMER features a good operational stability,
indicating that no significant leaching events occurred, and
that the enzyme remains stable under operation in flow. In
future, the presented HPLC-coupled flow system can be
used to screen the substrate scope of the amidohydrolase
MxcM for synthesis of imidazoline-containing, heterocyclic
compounds.
Figure 1: Residual activity of free (A) and immobilized MxcM (B) in phosphate buffer, n-hexane, MTBE, acetonitrile (ACN), and buffer with 20 vol% ACN.
Publications:
Winand, L.; Theisen, S.; Lütz, S.; Rosenthal, K.; Nett, M., Immobilization
of the Amidohydrolase MxcM and Its Application for Biocatalytic Flow
Synthesis of Pseudochelin A. Catalysts. 2023, 13(2), 229.
https://doi.org/10.3390/catal13020229
Contact:
lea.winand@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 79
Publications
2023
2021
Peer-reviewed Journal Articles
Peer-reviewed Journal Articles
• Winand, L.; Lernoud, L.; Meyners, S. A.; Kuhr, K.; Hiller, W.; Nett, M.
Myxococcus xanthus as Host for the Production of Benzoxazoles
ChemBioChem, 24, e202200635 (2023)
https://doi.org/10.1002/cbic.202200635
• Tippelt, A.; Nett, M.
Saccharomyces cerevisiae as Host for the Recombinant Production of
Polyketides and Nonribosomal Peptides
Microbial Cell Factories, 20, 161 (2021)
https://doi.org/10.1186/s12934-021-01650-y
• Winand, L.; Theisen, S.; Lütz, S.; Rosenthal, K.; Nett, M.
Immobilization of the Amidohydrolase MxcM and Its Application for
Biocatalytic Flow Synthesis of Pseudochelin A
Catalysts, 13, 229 (2023)
https://doi.org/10.3390/catal13020229
• Kruth, S.; Zimmermann, C. J.-M.; Kuhr, K.; Hiller, W.; Lütz, S.; Pietruszka, J.;
Kaiser, M.; Nett, M.
Generation of Aurachin Derivatives by Whole-Cell Biotransformation
and Evaluation of Their Antiprotozoal Properties
Molecules, 28, 1066 (2023)
https://doi.org/10.3390/molecules28031066
• Kruth, S.; Nett, M.
Aurachins, Bacterial Antibiotics Interfering with Electron Transport
Processes
Antibiotics, 12, 1067 (2023)
https://doi.org/10.3390/antibiotics12061067
• Steinmetz, T.; Lombe, B. K.; Nett, M.
Intermediates and Shunt Products of Massiliachelin Biosynthesis in
Massilia sp. NR 4-1
Beilstein Journal of Organic Chemistry, 19, 909-917 (2023)
https://doi.org/10.3762/bjoc.19.69
2022
Peer-reviewed Journal Articles
• Kinner, A.; Nerke, P.; Siedentop, R.; Steinmetz, T.; Classen, T.; Rosenthal,
K.; Nett, M.; Pietruszka, J.; Lütz, S.
Recent Advances in Biocatalysis for Drug Synthesis
Biomedicines, 10, 964 (2022)
https://doi.org/10.3390/biomedicines10050964
• Lombe, B. K.; Winand, L.; Diettrich, J.; Töbermann, M.; Hiller, W.; Kaiser,
M.; Nett, M.
Discovery, Biosynthetic Origin, and Heterologous Production of
Massinidine, an Antiplasmodial Alkaloid
Organic Letters, 24, 2935-2939 (2022)
https://doi.org/10.1021/acs.orglett.2c00963
• Vollmann, D. J.; Winand, L.; Nett, M.
Emerging Concepts in the Semisynthetic and Mutasynthetic
Production of Natural Products
Current Opinion in Biotechnology, 77, 102761 (2022)
https://doi.org/10.1016/j.copbio.2022.102761
• Kruth, S.; Schibajew, L.; Nett, M.
Biocatalytic Production of the Antibiotic Aurachin D in Escherichia coli
AMB Express, 12, 138 (2022)
https://doi.org/10.1186/s13568-022-01478-8
• Steinmetz, T.; Hiller, W.; Nett, M.
Amamistatins Isolated from Nocardia altamirensis
Beilstein Journal of Organic Chemistry, 18, 360-367 (2022)
https://doi.org/10.3762/bjoc.18.40.
• Vollmann, D. J.; Busche, T.; Rückert, C.; Nett, M.
Complete Genome Sequence of the Nonmotile Myxococcus xanthus
Strain NM
Microbiology Resource Announcements, 10, e00989-21 (2021)
https://doi.org/10.1128/MRA.00989-21
• Winand, L.; Sester, A.; Nett, M.
Bioengineering of anti-inflammatory natural products
ChemMedChem, 16, 767-776 (2021)
https://doi.org/10.1002/cmdc.202000771
• Winand, L.; Vollmann, D. J.; Hentschel, J.; Nett, M.
Characterization of a Solvent-Tolerant Amidohydrolase Involved in
Natural Product Heterocycle Formation
Catalysts, 11, 892 (2021)
https://doi.org/10.3390/catal11080892
• Winand, L.; Schneider, P.; Kruth, S.; Greven, N.-J.; Hiller, W.; Kaiser, M.;
Pietruszka, J.; Nett, M.
Mutasynthesis of Physostigmines in Myxococcus xanthus
Organic Letters, 23, 6563–6567 (2021)
https://doi.org/10.1021/acs.orglett.1c02374
SCIENTIFIC HIGHLIGHTS 2023
Industrial Chemistry (TC)
Page 80
SCIENTIFIC HIGHLIGHTS 2023
Page 81
Polymer-Grade Bio-Monomers from Oleochemicals by Combining Homogeneous
Catalysis and Selective Product Crystallization in an Integrated Process
Astrid Ina Seifert, Hannes Wegener, Katharina Brühl, Thomas Seidensticker, and Kerstin Wohlgemuth
As part of the global shift towards a sustainable chemical industry, it is essential to develop new chemical processes based
on renewable resources as an alternative to increasingly scarce fossil reserves. Oleo-chemicals, which are produced from
natural fats and oils, can be modified to have properties suitable for bio-based monomers for polymer production. They
have exceptionally high potential as drop-in solutions for conventional petrochemical monomers. Simultaneously, it is
essential to separate the catalyst and product phases downstream. This is necessary to meet purity requirements since
transition metals are often toxic. Additionally, it enables the recycling of expensive catalysts, making these processes
more economically viable. In this study, we combined a highly selective reaction with an innovative cooling crystallization
procedure to produce polymer-grade bio-monomers.
For the preparation of bio-based monomers, the substrate
methyl 10-undecenoate (C11-ME) is converted to the bifunctional 1,12-dimethyl dodecanedioate (l-C12-DME) via
palladium-catalyzed methoxycarbonylation (see Figure 1).
A cooling crystallization strategy was developed and implemented to obtain the monomer product in high purity
after the reaction step and to recycle the catalyst.
sion progress via CO gas consumption. By utilizing this setup, it was possible to transition from a time-dependent
reaction procedure to a conversion-dependent one. Figure 2 displays the results of a recycling experiment, where
80 % conversion were set and achieved in each run, prolonging the reaction time accordingly to reach this goal.
This consistency resulted in a nearly constant composition of the reaction solution, enabling optimal crystallization conditions
Figure 1: Reaction scheme of the homogeneously catalyzed methoxycarbonylation of
methyl 10-undecenoate (C11-ME) to linear 1,12-dimethyl dodecanedioate (l-C12-DME).
Previous studies have demonstrated the recyclability of
the catalyst and the excellent crystallization properties of
the desired product. However, these studies were developed separately. Therefore, a combination of the individual steps resulted in a reaction-crystallization setup that
enabled highly inert and effective coupling of the reaction,
crystallization, separation, and recycling steps. This setup
provides an excellent starting position for further optimization. Crystallization is a delicate process that is sensitive to minor changes in the composition of the reaction
solution. This change occurs over the course of several
recycling runs. Maintaining consistent product purity is a
significant challenge due to the accumulation of side
products and a decrease in substrate conversion. To address this challenge, a non-invasive reaction monitoring
system was implemented to track the reaction's conver-
Contact:
hannes.wegener@tu-dortmund.de
thomas.seidensticker@tu-dortmund.de
kerstin.wohlgemuth@tu-dortmund.de
Figure 2: Results of recycling with constant conversion (X = 80%) (left) Conversion
measured offline and online, and (right) composition of organic components in
the mixture before (left bars) and after (right bars) purification in the respective
recycling steps.
These optimized conditions resulted in product purities >
99.9 %, making them applicable in polymer synthesis.
The developed concepts and their combination resulted
in a setup that produces polymer-grade bio-monomers,
improving existing works and setting new grounds for
further studies.
Publications:
Seifert, A. I., Wegener, H. W., Brühl, K., Seidensticker, T.,
Wohlgemuth, K., (2023) "Polymer-Grade Bio-Monomers from
Oleochemicals by Combining Homogeneous Catalysis and
Selective Product Crystallization in an Integrated Process"
Processes, 11(10), 2861; DOI: 10.3390/pr11102861
SCIENTIFIC HIGHLIGHTS 2023
Page 82
Development of Eco-Friendly and Sustainable PET Glycolysis Using Sodium
Alkoxides as Catalyst
Saqib Javed and Dieter Vogt
The mounting environmental burden of postconsumer polyethylene terephthalate (PET) waste needs a more effective
recycling approach to combat global pollution and foster a circular economy. PET glycolysis offers a promising approach
by transforming PET into the valuable monomer bis(2-hydroxyethyl)terephthalate (BHET). However, conventional methods
rely on water-intensive processes, hindering catalyst stability and solvent reuse. Here, we introduced a "green" glycolysis
technique using sodium alkoxides and eliminating the need for an anti-solvent. Through response surface methodology,
we optimized reaction parameters to achieve high PET conversion and ethylene glycol (EG) recycling. Our approach also
demonstrates catalyst tolerance for colored and mixed PET waste, with sodium methoxide (MeONa) exhibiting superior
performance. Thus, the potential of BHET precipitation without the need for water, subsequent reuse of EG, and catalyst
tolerance in mixed PET waste provide a viable strategy to meet the future demands of waste recycling.
Most of the literature reported on PET glycolysis (homogeneously catalyzed) indicates the use of water as a precipitating agent to separate the BHET (the main product of
depolymerization via glycolysis). Water, on one hand,
serves as a precipitating agent (anti-solvent), while it also
dilutes the glycolysis mixture, making it easier to let the
reaction mixture flow out of the reaction vessel. However,
this added water needs to be evaporated in later steps.
Furthermore, water destroys the sodium alkoxides, the
glycolysis catalysts. From an industrial point of view, if no
water is added to EG, this solvent can be reused in the depolymerization, and the catalyst will also be saved from
water destruction, leading to the maximum utility of all resources. According to the experimental setup depicted in
Figure 1, BHET is directly precipitated from the EG solution
without adding water after the reaction.
ence of Na+ in the filtrate of various samples. To confirm
the catalytic activity, EG was recycled two times (R1 and
R2) and the results are comparable to the initial run for
both catalysts. The optimum recipe was also implemented
on green-colored PET waste and results showed that both
catalysts can also depolymerize colored PET waste. Furthermore, GR1 results show that both filtrates from colored PET waste were successfully recycled to get PET
conversion up to 95%. We have also implemented the optimized glycolysis procedure to mixed PET waste resulting
in substantial PET conversion signifying the potential of
both catalysts to recycle mixed PET waste.
Figure 1: Experimental setup for green glycolysis.
However, this method required the use of a large excess
of EG to PET, which was optimized via the design of the
experiment (DoE).
Afterwards, we implemented the optimum recipe for recycling the EG in the presence of sodium ethoxide (EtONa)
and sodium methoxide (MeONa), and the results are presented in Figure 2. Under similar reaction conditions, MeONa has better conversion than EtONa due to its better
catalytic activity. ICP measurements indicated the presPublication:
Javed, S; Vogt, D., Development of Eco-Friendly and Sustainable
PET Glycolysis Using Sodium Alkoxides as Catalysts, ACS
Sustainable Chem. Eng. 2023, 11, 11541−11547.
https://doi.org/10.1021/acssuschemeng.3c01872
Figure 2 Recycling of EG under optimized conditions.
From an industrial standpoint, if no water is added, EG can
be recycled without further processing. Additionally, it will
reduce the requirement for unit operations that involve
heating water first, followed by filtration and evaporation.
As a result, these characteristics make the PET depolymerization procedure more efficient and affordable.
Contact:
saqib.javed@tu-dortmund.de
dieter.vogt@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 83
Stable and Continuous Production of Amines via Reductive Amination in a Green
Switchable Solvent System with Efficient Water Removal
Tim Benjamin Riemer, Philipp Lapac, Dieter Vogt, Thomas Seidensticker
Homogeneous catalysis is central to sustainable chemistry since its high catalytic activity and selectivity allow efficient
reactant conversion into desired products. However, recycling the active catalyst complex poses significant challenges. At
the same time, it is often a crucial requirement for bringing new and potentially more sustainable processes from research
into application. An efficient way to achieve this is the utilization of thermomorphic multiphase systems (TMS). At reaction
temperature, the solution is monophasic, allowing reaction without transport limitation. Cooling after reaction reduces
the miscibility gap, and two phases are formed. One phase ideally contains the product, and the second phase contains
the catalyst, which, therefore, can be recycled through simple decantation. This work stands out with its comprehensive
approach, highlighting TMS’s potential as a catalyst recycling method for continuous chemical processes by demonstrating
exceptional performance in its critical areas, such as reaction yields, catalyst stability/retention, and co-product removal.
In this study, a novel continuous process for the homogeneously catalyzed reductive amination to aliphatic amines
in a green methanol-based TMS with simultaneous removal of the co-product water is presented.
Figure 1: Concept of the continuous TMS process with water removal.
The importance of continuous miniplant experiments
is emphasized as they allow for identifying and counteracting potential adverse effects of accumulating components early on. Despite this TMS already being applied
in hydroaminomethylation, unexpected challenges were
encountered in adapting the TMS to reductive amination
due to the formation of high amounts of the undesired
alcohol. Here, water accumulation in the recycle phase
was identified as a critical and enhancing factor for alcohol formation. Subsequent batch experiments revealed
Contact:
tim.riemer@tu-dortmund.de
dieter.vogt@tu-dortmund.de
thomas.seidensticker@tu-dortmund.de
the addition of carbon monoxide to the gas phase as the
most effective measure against alcohol formation, even
in the presence of water. By transferring these results to
the miniplant operation, over the entire operation period
of over 90 hours, high yields of over 90% to the tertiary
product amine were achieved by controlling the CO content in the gas phase. In addition to the high amine selectivities of up to 96.5%, an outstanding stable and efficient
membrane operation was performed, leading to a steadystate water concentration of less than 3.1 wt.%. In addition
to water removal via the membrane, the stability of the
process is largely dependent on the amount of catalyst
loss, which can occur both via the permeate stream of the
membrane and the product phase stream. In total, only
0.6 mg of rhodium per kg product amine was lost over the
miniplant operation. Since membrane rejections of over
99.7% of the valuable catalyst were maintained, only 0.9
wt% of the initial rhodium mass was lost over the membrane. Despite the excellent membrane performance, its
catalyst loss was still outperformed by the TMS, with only
33 ppb rhodium in the product phase and <0.2 mg rhodium per kg of produced product amine. This way, a leaching rate of only 0.003 %/h of the initial rhodium mass over
the product phase was achieved. To our knowledge, this
is the lowest recorded leaching in continuous thermomorphic multiphase systems. For evaluation of the overall process performance, the reaction yields, the catalyst
stability, and retention, the water discharge over the OSN
membrane, and the stability of the membrane operation
must be taken into account. Here, for the first time, excellent performance in each of those areas has been demonstrated, which gives an optimistic outlook for the potential
of the proposed green TMS in chemical processes.
Publication:
Riemer, T. B.; Lapac, P.; Vogt, D.; Seidensticker, T., Stable and
Continuous Production of Amines via Reductive Amination in a
Green Switchable Solvent System with Efficient Water Removal.
ACS Sustainable Chem. Eng. 2023, 11 (35), 12959–12966.
https://doi.org/10.1021/acssuschemeng.3c02320
SCIENTIFIC HIGHLIGHTS 2023
Page 84
Continuous production of amines directly from alkenes via cyclodextrin-mediated
hydroaminomethylation using only water as the solvent
Thomas Roth, Rebecca Evertz, Niklas Kopplin, Sébastien Tilloy, Eric Monflier, Dieter Vogt and Thomas Seidensticker
Homogeneous transition metal catalysts offer many strengths, including high catalyst activity and selectivity even at
comparatively mild operating conditions. Despite these advantages, homogeneous catalysts are not used in most largescale industrial processes, as separation is complex and therefore cost-intensive. Since recycling of the transition metals is
indispensable for the economic and ecological sustainability of processes using homogeneous catalysts, the development
of efficient separation and recycling concepts is required to make use of their strengths. The immobilization of the catalyst
in multiphase systems offers a promising approach in this respect, as the catalyst phase can be separated and recycled
with relatively low effort. However, this approach also poses certain challenges, such as mass transport limitations across
the phase interface, which makes the use of intensification strategies imperative. Various intensification strategies are
discussed in the literature, but are usually not evaluated under scale-up and continuous conditions. Therefore, a particularly
promising intensification strategy for continuous processes using aqueous multiphase systems for homogeneously
catalyzed carbonylation reactions is investigated and optimized in this research work.
Hydroaminomethylation (HAM), a tandem reaction of hydroformylation and reductive amination, is an atom-economic route for the efficient production of amines in a single reaction step, starting from basic chemicals such as
alkenes (Figure 1). Herein we present the first successful
establishment of a continuous process for HAM in an
aqueous multiphase system.
Figure 1: General scheme of the hydroaminomethylation based on a 1-alkene and
a secondary amine.
The green mass transfer agents randomly methylated-ß-cyclodextrins (CD) enabled the catalytic system consisting of rhodium/sulfoXantphos to achieve high yields of
up to 70% with selectivities of up to 80% in several continuous experiments with a total run time of more than 220 h.
The key here is that water and products have large polarity
differences, but the reaction still proceeds effectively due
to the addition of cyclodextrin (Figure 2), which made the
application of further organic solvents obsolete.
Figure 2: Proposed mechanism for cyclodextrin-mediated reaction systems (left).
Basic process design for the recycling of homogeneous catalysts using aqueous
biphasic reaction systems (right).
Publication:
Roth, T., Evertz, R., Kopplin, N., Tilloy, S., Monflier, E., Vogt, D.,
Seidensticker, T., Continuous production of amines directly from alkenes
via cyclodextrin-mediated hydroaminomethylation using only water as
the solvent Green Chem., 2023, 25, 3680-3691., 2023, 25, 3680-3691,
The main achievements in this way were the investigation
of the influence of the randomly methylated-ß-cyclodextrin concentration on the reaction rate and the selectivity
in batch studies. In continuous experiments, various operating conditions such as reaction and separation temperature, residence time, stirrer speed and different substrate ratios were optimized on-stream (Figure 3). In a final
experiment it was shown that high yields of >70% can be
achieved while the catalyst loss in the product phase is
enormously small at 0.003% h−1 of the initial mass, which
is the lowest ever reported value for the HAM on this scale.
Within a run time of 78 hours, 2.87 kg of tertiary amine
were produced using only 0.2 g of transition metal, while
the loss of rhodium per kg of product produced was mostly around 0.15 mg kg−1, suggesting possible economical
applicability.
Figure 3: Yields for continuously operated hydroaminomethylation of 1-octene
with diethylamine during parameter optimization on stream.
Contact:
thomas2.roth@tu-dortmund.de
dieter.vogt@tu-dortmund.de
thomas.seidensticker@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 85
Publications
2023
Journal Articles
• Seifert, A. I., Wegener, H. W., Brühl, K., Seidensticker, T., Wohlgemuth, K.
Polymer-Grade Bio-Monomers from Oleochemicals by Combining
Homogeneous Catalysis and Selective Product Crystallization in an
Integrated Process
Processes, 11 (10), 2861 (2023)
https://doi.org/10.3390/pr11102861
• Riemer, T. B., P. Lapac, P., Vogt, D., Seidensticker, T.
Stable and Continuous Production of Amines via Reductive Amination
in a Green Switchable Solvent System with Efficient Water Removal
ACS Sustainable Chem. Eng., 11, 12959–12966 (2023)
https://doi.org/10.1021/acssuschemeng.3c02320
• Javed, S., Ropel, D., Vogt, D.
Sodium ethoxide as an environmentally benign and cost-effective
catalyst for chemical depolymerization of post-consumer PET waste,
Green Chem., 25, 1442-1452 (2023)
https://doi.org/10.1039/D2GC04548F
• Javed, S., Vogt, D.
Development of Eco-Friendly and Sustainable PET Glycolysis Using
Sodium Alkoxides as Catalysts
ACS Sustainable Chem. Eng., 11, 31, 11541–11547 (2023)
https://doi.org/10.1021/acssuschemeng.3c01872
• Vondran, J., Moeschke, R., Deysenroth, T., Seidensticker, T.
Pushing Boundaries—Selective Cooling Crystallization as Tool
for Selectivity Compensation and Product Purification Using a
Recyclable Pd/Xantphos Catalyst in the Methoxycarbonylation of
Methyl 10-Undecenoate
Eur. J. Lipid Sci. Technol., 125, 2200126 (2023)
https://doi.org/10.1002/ejlt.202200126
• Heider, C., Menk, M., Terhorst, M., Vogt, D., Seidensticker, T.
Synthesis of Tertiary Fatty Amines in Water: The Dual Role
of Dimethylamine as Reagent and Phase Mediator in the
Homogeneously Catalyzed Fatty Alcohol Amination
ACS Sustainable Chem. Eng. 11, 31, 11359–11363 (2023)
https://doi.org/10.1021/acssuschemeng.3c02764
• Diekamp, J., Seidensticker, T.
Synthesis Strategies towards Tagged Homogeneous Catalysts To
Improve Their Separation
Angew. Chem. Int. Ed. , e202304223 (2023)
DOI: 10.1002/anie.202304223
• Roth, T., Evertz, R., Kopplin, N., Tilloy, S., Monflier, E., Vogt, D.,
Seidensticker, T
Continuous production of amines directly from alkenes via
cyclodextrin-mediated hydroaminomethylation using only water as
the solvent
Green Chem., 25, 3680-3691(2023)
https://doi.org/10.1039/D2GC04847G
• Kampwerth, A., Terhorst, M., Kampling, N., Vogt, D., Seidensticker, T.
Synthesis of biobased amines via Pd-catalysed telomerisation of the
renewable β-myrcene in a water/ethanol multiphase system: catalyst
recycling enabled by a self-separating product phase
Green Chem. 25, 6345-6354, (2023)
https://doi.org/10.1039/D3GC00453H
• Heider, C., Winter, A., Voß, V., Vogt, D., Seidensticker, T.
Homogeneous Catalysis at its Edge: High-Temperature Ru-Catalysed
Amination of Alcohols under Continuous Flow Conditions
ChemCatChem, 15 (5), e202201307 (2023)
https://doi.org/10.1002/cctc.202201307
• Metzger, J. O., Biermann, U., Seidensticker, T.
Fats and Oils as Renewable Feedstock for the Chemical Industry
Eur. J. Lipid Sci. Technol. 125 (5), 2300038 (2023)
https://doi.org/10.1002/ejlt.202300038
• Javed, S., Vogt, D.
Kinetic Investigation for Chemical Depolymerization of PostConsumer PET Waste Using Sodium Ethoxide
Ind. Eng. Chem. Res. 62(10), 4328–4336 (2023)
https://doi.org/10.1021/acs.iecr.2c04308
• von Vietinghoff, N., Immken, A., Seidensticker, T., de Caro, P., Thiebaud
Roux, S., Agar, D. W.
Gas Introduction by Permeation into Long Fluorinated Ethylene
Propylene Capillaries with Slug Flow
Chem Eng Technol, 46 (5), 1047-1051 (2023)
https://doi.org/10.1002/ceat.202200557
• Javed, S., Fisse, J., Vogt, D.
Optimization and Kinetic Evaluation for Glycolytic Depolymerization
of Post-Consumer PET Waste with Sodium Methoxide
Polymers 15 (3), 687 (2023)
DOI: 10.3390/polym15030687
SCIENTIFIC HIGHLIGHTS 2023
Page 86
2022
2021
• Hares, K., Vogelsang, D., Wernsdörfer, C.S., Panke, D., Vogt, D.,
Seidensticker, T.
Palladium-catalyzed synthesis of mixed anhydrides via carbonylative
telomerization
Catal. Sci. Technol., 12, 3992-4000 (2022)
https://doi.org/10.1039/D2CY00486K
• Söderholm, V., Esteban, J., Vogt, D.
Synthesis of a H-Sulfo-POSS catalyst and application in the
acetalization of glycerol with 2-butanone to yield a biofuel additive
Catal. Sci. Technol. 11, 4529-4538 (2021)
https://doi.org/10.1039/D1CY00344E
• Vondran, J., Benninghoff, T., Emminghaus, A.I., Seidensticker, T.
Catalytic Synthesis of Methyl 9,10-dihydroxystearate from Technical
Feedstocks in Continuous Flow via Epoxidation and Hydrolysis
Eur. J. Lipid Sci. Technol. 124(7), 2200041 (2022)
https://doi.org/10.1002/ejlt.202200041
• Vondran, J., Pela, J., Palczewski, D., Skiborowski, M., Seidensticker, T.
Curse and Blessing–The Role of Water in the Homogeneously
Ru-Catalyzed Epoxidation of Technical Grade Methyl Oleate
ACS Sustainable Chem. Eng. 9 (34), 11469–11478 (2021)
https://doi.org/10.1021/acssuschemeng.1c03573
• Huxoll, F., Kampwerth, A., Seidensticker, T., Vogt, D., Sadowski, G.
Predicting Solvent Effects on Homogeneity and Kinetics of the
Hydroaminomethylation: A Thermodynamic Approach Using PC-SAFT
Ind. Eng. Chem. Res. 61, 5, 2323–2332 (2022)
https://doi.org/10.1021/acs.iecr.1c03891
• Vondran, J., Furst, M.R.L., Eastham, G.E., Seidensticker, T., ColeHamilton, D.J.
Magic of Alpha: The Chemistry of a Remarkable Bidentate Phosphine,
1,2-Bis(di-tert-butylphosphinomethyl)benzene
Chem. Rev. 121(11) 6610–6653, (2021)
https://doi.org/10.1021/acs.chemrev.0c01254
• Vondran, J., Seifert, A.I., Schäfer, K., Laudanski, A., Deysen, T.,
Wohlgemuth, K., Seidensticker, T.
Progressing the Crystal Way to Sustainability: Strategy for Developing
an Integrated Recycling Process of Homogeneous Catalysts by
Selective Product Crystallization
Ind. Eng. Chem. Res. 61(27), 9621–9631 (2022)
https://doi.org/10.1021/acs.iecr.2c00476
• Künnemann, K. U., Weber, D., Becquet, C., Tilloy, S., Monflier, E.,
Seidensticker, T., Vogt, D.
Aqueous Biphasic Hydroaminomethylation Enabled by Methylated
Cyclodextrins: Sensitivity Analysis for Transfer into a Continuous
Process
ACS Sustainable Chem. Eng., 9, 273–283 (2021)
https://doi.org/10.1021/acssuschemeng.0c07125
• Heider, C., Pietschmann, D., Vogt, D., Seidensticker, T.
Selective Synthesis of Primary Amines by Kinetic-based Optimization
of the Ruthenium-Xantphos Catalysed Amination of Alcohols with
Ammonia
ChemCatChem, 14 (18), e202200788 (2022)
DOI: 10.1002/cctc.202200788
• Huxoll, F., Jameel, F., Bianga, J., Seidensticker, T., Stein, M., Sadowski, G.,
Vogt, D.
Solvent Selection in Homogeneous Catalysis – Optimization of
Kinetics and Reaction Performance
ACS Catal., 11, 590–594, (2021)
https://doi.org/10.1021/acscatal.0c04431
• Vondran, J., Peters, M., Schnettger, A,. Sichelschmidt, C., Seidensticker, T.
From tandem to catalysis – organic solvent nanofiltration for catalyst
separation in the homogeneously W-catalyzed oxidative cleavage of
renewable methyl 9,10-dihydroxystearate
Catal. Sci. Technol., 12, 3622-3633 (2022)
https://doi.org/10.1039/D1CY02317A
• Schlüter, S., Künnemann, K. U., Freis, M., Roth, T., Vogt, D., Dreimann, J.
M., Skiborowski, M.
Continuous co-product separation by organic solvent nanofiltration for
the hydroaminomethylation in a thermomorphic multiphase system
Chem. Eng. J., 409, 128219 (2021)
https://doi.org/10.1016/j.cej.2020.128219
SCIENTIFIC HIGHLIGHTS 2023
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SCIENTIFIC HIGHLIGHTS 2023
Thermodynamics (TH)
Page 88
SCIENTIFIC HIGHLIGHTS 2023
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Continuous Non-Centrifugal Phase Separation in Biphasic Whole-Cell Biocatalysis
Applied Catastrophic Phase Inversion on a Lab-Scale Prototype.
Lisa Janssen, Gabriele Sadowski, Christoph Brandenbusch
Within several chemical and biotechnological processes, the presence of particles (e.g. as catalyst) in a biphasic reaction
system (oil/water) often leads to the formation of stable Pickering type emulsions, hindering cost-efficient and effective
downstream processing. State-of-the-art-concepts for phase separation fail or include inefficient and costly strategies
(centrifugation / de-emulsifiers). Using the phenomenon of catastrophic phase inversion (CPI), efficient phase separation
can be achieved by addition of dispersed phase. Based on a patent filed at TU Dortmund, a process concept (termed:
Applied Catastrophic Phase Inversion; ACPI) was developed, enabling continuous phase separation of stable emulsion by
using the CPI phenomenon. A fully automated pilot-scale prototype was planned and constructed and applicability of the
concept to different biocatalysts and aqueous/organic systems confirmed.
Depending on their wettability, cells / particles will either
stabilize oil in water, or water in oil emulsions. Wettability is
thereby characterized by the three-phase contact angle ow
measured through the aqueous phase (see Fig. 1). The particle stabilized, also termed Pickering-type emulsions,
can undergo a phenomenon called catastrophic phase inversion, being the sudden switch of emulsion types from
an oil/water to a water/oil emulsion (or vice versa). This inversion is achieved by addition of dispersed phase exceeding a critical volumetric threshold. This catastrophic
phase inversion (CPI) is accompanied by a complete destabilization of the emulsion.
biocatalysts (Escherichia coli JM101 and Pseudomonas
putida KT2440). The critical volumetric phase ratio of organic to water phase (Vo:Vw) which has to be applied to
achieve phase inversion, was calculated based on the
guideline developed in our previous work.
Figure 2: Picture of the lab-scale ACPI prototype as constructed within this work.
Figure 1: Attachment of particles with three-phase contact angle ow to a planar
organic/water interface. (Left) Spherical particles with radius R. (Right) Nonspherical, rod-shape, particles / cells with rod length a, and rod radius b.
Within this work, we designed and constructed a fully automated lab-scale prototype (see Fig. 2) for c o n t i n u ous phase separation adhering to the CPI principle. We
demonstrate the applicability of the concept for various
long-term stable bioprocess-derived Pickering-type emulsions, investigating the influence of both, different organic
solvents (n-heptane, ethyl oleate and 1-octanol) as well as
Contacts:
lisa2.janssen@tu-dortmund.de
christoph.brandenbusch@tu-dortmund.de
gabriele.sadowski@tu-dortmund.de
A process window that allowed for reliable operating conditions was defined. We investigated the influence of process
parameters (e.g., flow rates) on stability and success of the
(continuous) phase separation. Furthermore, we investigated the robustness towards perturbations (e.g., fluctuation
in water/organic phase ratio of the feed emulsion).
A phase separation efficiency of over 96 % could be
achieved for all emulsions considered within this work.
ACPI thus is an innovative and universal tool, overcoming
the limitations of the drawbacks in classical downstream
processing concepts used in state-of-the-art processing
of bioprocess-derived Pickering-type emulsions.
Publications:
Janssen, L.; Sadowski, G.; Brandenbusch, C. Continuous Phase
Separation of Stable Emulsions from Biphasic Whole-cell
Biocatalysis by Catastrophic Phase Inversion. Biotechnology
journal 2023, 18 (6). https://doi.org/10.1002/biot.202200489
SCIENTIFIC HIGHLIGHTS 2023
Page 90
Effects of solvent and of catalyst on the acid-catalyzed esterification of levulinic
acid via activity-based models
Marcel Klinksiek, Sindi Baco, Christoph Held
This study focuses on understanding the kinetics and thermodynamics of the esterification of levulinic acid with ethanol.
So far, thermodynamic models have been used to predict solvent influences on reaction rates and reaction yields. The idea
of this work was to also consider the catalyst activity in the kinetic model. Accessing catalyst activity with the model ePCSAFT allowed the first time to precisely predict the catalyst effects on reaction rates.
When considering the transition from a fossil-fuel based
economy to a sustainable one, biomass valorization
represents a promising strategy. Increasing the knowledge
in the catalyst-kinetics-thermodynamics relation allows
understanding and improving the efficiency of biomass
conversion, e.g. into levulinic acid (LA) or ethyl levulinate
(ELA). In general, ELA is synthesized via an acid-catalyzed
esterification reaction of LA with an excess amount of ethanol (Eqs. 1 & 2).
interactions with the reaction components. The resulting
equation describes the reaction rate r by
where x, Y and Kth describe the mole fractions, the activity
coefficients and the thermodynamic equilibrium constant, respectively. This approach incorporates the dissociation of H2SO4 in the reaction mixture, which we solved in
order to predict proton activity (aH3O+) along the reaction
coordinate using ePC-SAFT.
The solvent influences H2SO4 dissociation, reaction kinetics, catalyst activity and reaction equilibrium. We studied
the influence of the green solvent GVL (Y-valerolactone)
and of the H2SO4 concentration on reaction kinetics of (1)
(see Figure 1).
Figure 2: Rate constants k1 for selected conditions at 333 K. Green: exp. data,
Black: ePC-SAFT prediction using one experiment as reference (shaded, “ref”).
Exact conditions: See publication.
Figure 1: Ethyl levulinate mole fraction during the esterification reaction without
cosolvent (black, "ref"), with GVL cosolvent (blue, "3"), with GVL cosolvent and
reduced catalyst concentration (red, "4") at 333 K. Symbols: Exp. data, lines: ePCSAFT predictions. Exact conditions: See publications.
The kinetics of LA esterification in the cosolvent-free system (black) appears to be the fastest, followed by the reaction under GVL addition. Decreased amount of catalyst
reduces the reaction kinetics. This behavior has been confirmed by an ePC-SAFT prediction. For the latter, we developed an activity-based model to account for the catalyst
Publications:
Klinksiek, M.; Baco, S; Leveneur, S.; Legros, J.; Held, C., Activitybased models to predict kinetics of levulinic acid esterification,
ChemPhysChem 2023, 24, e202200729
https://doi.org/10.1002/cphc.202200729
Figure 2 compares experimental and predicted rate
constants k1 at various experimental conditions (see
figure caption of Figure 1). The results show that the activity-based model is capable of predicting the catalyst
effect on the reaction rate. Only one reference experimental k1 ("ref.") was required to predict the influence of
catalyst and cosolvent on the kinetics. This was possible
at the different conditions (2-6) concerning the cosolvent
or catalyst concentration. To conclude, we were able to
predict kinetics in an arbitrarily chosen reaction environment concerning solvent, catalyst, and any concentration
by combining proton activity, dissociation equilibria and
reactant activities from ePC-SAFT into a reaction kinetics
approach.
Contact:
christoph.held@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 91
Modeling the impact of tablet surface layers on the dissolution rate in water
Stefanie Dohrn, Gabriele Sadowski
This study utilized thermodynamic modeling to understand the behavior of amorphous solid dispersion (ASD) tablets
during dissolution when exposed to water. It emphasizes the importance of the interfacial surface layers formed during
dissolution and predicts drug load (DL)-dependent loss of release (LoR) that often prevents the complete dissolution
of the tablet in water. The reasons for this are crystallization and/or liquid-liquid phase separation (LLPS) at the tablet
surface. To this end, the phase behavior and glass transition of tablets composed of the drugs naproxen or venetoclax
and of poly(vinylpyrrolidone-co-vinyl acetate) (PVPVA64) in contact with water were predicted using the Perturbed-Chain
Statistical Associating Fluid Theory (PC-SAFT) and the Gordon-Taylor equation. The modeling results were found to be in
perfect agreement with (non)dissolution experiments.
According to the concept depicted in Figure 1, the behavior of tablets in contact with water is influenced by water
sorption, LLPS, crystallization, and the viscosity of the gel
layer formed, impacting the dissolution performance.
Phase changes can lead to surface passivation. The LoR
mechanisms were categorized into two types, depending
on whether the passivation is primarily driven by drug
crystallization (LoR Type I) or LLPS (LoR Type II).
time (Figure 2). The predicted tablet/water phase behavior
(Figures 3a and 3b) and DL-dependent phase transition at
the tablet/water surface could experimentally be validated via microscopy images (Figures 3c-h).
Figure 1: Schematic tablet/water surface of (a) LoR Type I and (b) Type II.
The DL-dependent release mechanisms for PVPVA64-based naproxen (LoR Type I) and venetoclax (LoR
Type II) ASDs were predicted and experimentally investigated (Figures 2 and 3).
Figure 3: Ternary phase diagrams at 37 °C of (a) LoR Type I system: naproxen/
PVPVA64/water and (b) LoR type II system: venetoclax/ PVPVA64/water. The
green dashed lines represent the glass transition; the orange lines represent the
solubility lines; the black lines represent the LLPS boundaries with gray tie lines;
and the blue, yellow, and red straight lines represent the hydration pathways for
different DLs. Tablet images after 40 min dissolution for DLs (c) 10 wt%, (d) 20 wt%,
and (e) 30 wt% naproxen and (f) 0.5 wt%, (g) 1 wt%, and (h) 2.5 wt% venetoclax.
Figure 2: Release profile of naproxen at 37 °C from a naproxen/PVPVA64 ASD, with
DLs of 10 wt % (blue circles), 20 wt % (yellow squares), and 30 wt % (red triangles).
The predictions were in excellent agreement with experimentally observed layer formation and its impact on the
dissolution. It turned out that the drug-release levels
strongly decreased with increasing DL. While the 10 wt %
DL tablets released 60% of the naproxen, the 30 wt% DL
tablets released only 10% of the naproxen at the same
Contacts:
stefanie.walter@abbvie.com
gabriele.sadowski@tu-dortmund.de
The presented modeling approach supports the understanding of a tablet release mechanism during dissolution
and helps to identify the maximum DL of a tablet, which allows high drug release without undergoing phase changes
during dissolution.
Publication:
Dohrn S.; Kyeremateng S.O.; Bochmann E.; Sobich E.; Wahl A.;
Liepold B.; Sadowski G.; Degenhardt. M., Thermodynamic Modeling
of the Amorphous Solid Dispersion-Water Interfacial Layer and Its
Impact on the Release Mechanism, Mol. Pharmaceutics 2023, 15
(5), 1539. doi:10.3390/pharmaceutics15051539
SCIENTIFIC HIGHLIGHTS 2023
Page 92
Carboxylation of Acetylene without Salt Waste: Using thermodynamic predictions
to optimize the catalyst and the reaction solvent
Christoph Held, Daniel Schick, Tim van Lingen, Lukas Gooßen, Gabriele Sadowski
The utilization of CO2 as C1 building block is a key towards a sustainable industrial synthesis of base chemicals. In this
work, we developed a circular process for the production of the C4 chemical dimethyl succinate from CO2 and acetylene,
i.e. a C-H carboxylation reaction. The inherent formation of salt waste in such C-H carboxylations has so far been a major
challenge. This was resolved in this work by esterification of the carboxylate product using methanol. The challenge of
enabling a one-pot synthesis in such a reaction sequence is to find reaction conditions that are efficient for all reaction
steps. Here, we applied ePC-SAFT to screen the reaction solvent and the base salt for the reaction to reach high solubility
of both the salt base and the reactants.
Conventionally, C4 chemicals are synthesized from acrylic
acid, propylene oxide, butane or ethylene, i.e. by coupling
building blocks C3 + C1, C2 + C1 or directly using C4 units.
In contrast, we were aiming at a route that uses CO2 as a
building block. However, it is known that it is very hard to
activate CO2 due to its thermodynamic low energetic level.
Thus, a very common way to activate CO2 is using molecular hydrogen to produce formic acid. In contrast, in this
work we used CO2 as a building block for a carboxylation
reaction. A concept has been developed (c.f. Fig. 1) over the
last years to carboxylate an alkyne, and we chose the example of acetylene carboxylation, yielding the C4- based
chemical dimethyl succinate.
salt base and the reactants acetylene and CO2. Without fitting parameters, ePC-SAFT identified N-methyl-2-pyrrolidone (NMP) as most efficient solvent, c.f. Fig. 2. NMP provides high solubility for CO2 and for acetylene, outperforming
the other solvents (water, methanol, acetonitrile, THF). ePCSAFT predicted that Cs2CO3 had the highest solubility in
NMP among the considered carbonate bases.
Figure 1: Synthetic entries to difunctionalized C4-commodities.
Figure 2: ePC-SAFT predicted solubility of gases at carboxylation conditions
(T = 100 °C; p = 10 bar) and esterification conditions (T = 200 °C; p = 72 bar) and
solubility of salts (T = 25°C). Solid bars represent solubilities in pure solvents.
Striped bars is gas solubility in solvent + Cs2CO3. Whenever the experimental
amount of added salt (dark red bar) is lower than its solubility, the dark red bar is
extended with a light red bar which represents the maximum solubility.
Our concept for sustainable C4 synthesis was as follows:
At moderate CO2 pressures, acetylene is doubly carboxylated, which requires basic conditions. The subsequent esterification of the succinate salt with methanol allowed
regenerating the base salt. Realizing a one-pot synthesis
of this concept requires a solvent that is efficient for all reaction steps. This solvent must provide high solubility of the
Publication:
Van Lingen, T.; Bragoni, V.; Dyga, M.; Exner, B.; Schick, D.; Held, C.;
Sadowski, G.; Goossen, L., Carboxylation of Acetylene without
Salt Waste: Green Synthesis of C4 Chemicals Enabled by a
CO2-Pressure Induced Acidity Switch. Angewandte Chemie I.E.
e202303882, doi.org/10.1002/anie.202303882
Summing up, our concept shown in Fig. 1 provides the proof
of concept for a salt-free route to C4 chemicals based on
CO2 as C1 building block, and could potentially be used to
valorize biogas (CH4/CO2).
ePC-SAFT proved to be efficient for optimizing the reaction medium of the one-pot synthesis of the C4 chemical
from CO2 by suggesting the optimal reaction solvent NMP
and the optimal base Cs2CO3.
Contacts:
christoph.held@tu-dortmund.de
gabriele.sadowski@tu-dortmund.de
SCIENTIFIC HIGHLIGHTS 2023
Page 93
Direct Generation of Compressed Air from Waste Heat by Cascaded
Thermocompressors with Self-Excited Overdriven Free Displacers
Analytical and Numerical Analysis
Fabian Fischer, Sebastian Peveling, Hans-Detlev Kühl
Compressed air is a widely used but expensive and inefficient industrial energy source. At the same time, large amounts of
waste heat remain unused. In order to exploit and utilize this waste heat potential at low production and operating costs,
a novel concept based on reciprocating thermocompressors has been developed. It focusses on maximum constructional
simplicity by arranging a cascade of identical stages, and on the application of self-excited, overdriven free displacers, the
frequencies of which may adapt independently of the pressure to ensure optimum operation of all stages, while largely
maintaining or even exceeding thermal similarity to the first stage. In order to prove the feasibility of such a system, it has
been investigated by means of an analytical and a numerical analysis.
The basic layout of a reciprocating thermocompressor
shows similarities to a β- or γ-type Stirling engine, in which
a pair of check valves replaces the power piston. Thus, the
air to be compressed simultaneously acts as the working
fluid of an open cycle. Figure 1 shows the schematic arrangement of two consecutive stages k and k+1 within a
cascade. Their reciprocating displacers periodically relocate the air between the hot and cold cylinder volumes via
a duct consisting of a cooler, a regenerator and a heater.
During the downward motion, the pressure is raised due to
isochoric heating, until it reaches the outlet pressure.
From then on, it remains constant, since the outlet valves
open and discharge the air into the upward buffer volume.
At the end of stroke, the displacers hit elastic limit stops,
so that their motion is reversed, preserving their kinetic
energy in the ideal case. The outlet valves close, and the
pressure drops due to cooling, until the inlet valves open
and air from the downward buffer enters the cycle volume.
At the lower end of stroke, the displacers once again
bounce back elastically, and the cycle is closed. As the displacer rod periodically plunges into the cold cylinder, the
overall cycle volume varies, and p,V-work is generated.
When properly designed, this work compensates any
friction losses, thus eliminating the need for external
actuation.
All relevant operating parameters, such as the conveyed
mass of air, the heat absorbed and the exergy gain of the
compressed air flow, depend on the stage pressure ratio
in such a way that a self-controlled steady-state operation
can be expected. The results obtained with an analytical
model indicate that such stable operating points exist
above a critical stage pressure ratio.
To further investigate the operating characteristics, a
three-stage cascade was modelled in Simulink® with its
extension SimscapeTM. Figure 2 exemplarily shows the
exergy gain of the compressed air flow as a function of the
total pressure ratio for the single stages k and for the entire cascade. The simulation results confirm the expected
stable operation of all stages for a wide range of total
pressure ratios as well as the existence of lower stability
limits, where the lowest operating stage stops.
Figure 2: Exergy gain ΔĖ of the compressed air flow (total and for each stage k of
the three-stage cascade) vs. total pressure ratio Πtot.
The results demonstrate that the presented concept is
a promising approach to generate compressed air from
waste heat in a both economically and ecologically advantageous way, and therefore strongly suggest further
experimental investigations as the next step.
Figure 1: Schematic drawing of two stages of a cascade of identical overdriven
free-displacer thermocompressors.
Contacts:
fabian2.fischer@tu-dortmund.de
sebastian.peveling@tu-dortmund.de
hans-detlev.kuehl@tu-dortmund.de
Publication:
Fischer, F.; Peveling, S.; Kühl, H.-D., Simulation and stability analysis
of a thermocompressor cascade with overdriven free displacers.
Thermal Science and Engineering Progress 2023, 44, 102037.
https://doi.org/10.1016/j.tsep.2023.102037
SCIENTIFIC HIGHLIGHTS 2023
Page 94
Publications
2023
• Kroll, P.; Exner, L.; Brandenbusch, C.; Sadowski, G.
Influence of Hydrophobic and Hydrophilic Chain Length of CiEj
Surfactants on the Solubilization of Active Pharmaceutical
Ingredients.
Molecular pharmaceutics 2023, 20 (2), 1296-1306.
https://doi.org/10.1021/acs.molpharmaceut.2c00941
• Dohrn, S.; Kyeremateng, S. O.; Bochmann, E.; Sobich, E.; Wahl, A.; Liepold,
B.; Sadowski, G.; Degenhardt, M.
Thermodynamic Modeling of the Amorphous Solid Dispersion-Water
Interfacial Layer and Its Impact on the Release Mechanism.
Pharmaceutics 2023, 15 (5).
https://doi.org/10.3390/pharmaceutics15051539
• Klinksiek, M.; Baco, S.; Leveneur, S.; Legros, J.; Held, C.
Activity-based Models to Predict Kinetics of Levulinic Acid
Esterification.
ChemPhysChem 2023, 24 (4).
https://doi.org/10.1002/cphc.202200729
• Lingen, T. van; Bragoni, V.; Dyga, M.; Exner, B.; Schick, D.; Held, C.;
Sadowski, G.; Gooßen, L. J.
Carboxylation of Acetylene without Salt Waste: Green Synthesis of C4
Chemicals Enabled by a CO2-pressure Induced Acidity Switch.
Angewandte Chemie International edition 2023, 62 (27).
https://doi.org/10.1002/anie.202303882
• Ascani, M.; Sadowski, G.; Held, C.
Simultaneous Predictions of Chemical and Phase Equilibria in
Systems with an Esterification Reaction Using PC-SAFT.
Molecules 2023, 28.
https://doi.org/10.3390/molecules28041768
• Anjum, F.; Wessner, M.; Sadowski, G.
Membrane-Based Solvent Exchange Process for Purification of API
Crystal Suspensions.
Membranes 2023, 13 (3), 263.
https://doi.org/10.3390/membranes13030263
• Grönniger, B.; Fritschka, E.; Fahrig, I.; Danzer, A.; Sadowski, G.
Water Sorption in Rubbery and Glassy Polymers, Nifedipine,
and Their ASDs.
Molecular pharmaceutics 2023, 20 (4), 2194–2206.
https://doi.org/10.1021/acs.molpharmaceut.3c00006
• Yu, G.; Gajardo-Parra, N. F.; Chen, M.; Chen, B.; Sadowski, G.; Held, C.
Aromatic Volatile Organic Compounds Absorption with Phenyl-based
Deep Eutectic Solvents: A Molecular Thermodynamics and Dynamics
Study.
AIChE journal / American Institute of Chemical Engineers 2023, 69 (5).
https://doi.org/10.1002/aic.18053
• Cordier, A.; Klinksiek, M.; Held, C.; Legros, J.; Leveneur, S.
Biocatalyst and Continuous Microfluidic Reactor for an Intensified
Production of N-Butyl Levulinate : Kinetic Model Assessment.
Chemical engineering journal 2023, 451.
https://doi.org/10.1016/j.cej.2022.138541
• Grönniger, B.; Danzer, A.; Kimpe, K.; Singh, A.; Sadowski, G.
Viscoelastic Behavior of Supercooled and Glassy ASDs at Humid
Conditions Can Be Predicted.
Molecular pharmaceutics 2023, 20 (5), 2568–2578.
https://doi.org/10.1021/acs.molpharmaceut.3c00008
• Krummnow, A.; Danzer, A.; Voges, K.; Kyeremateng, S. O.; Degenhardt, M.;
Sadowski, G.
Kinetics of Water-Induced Amorphous Phase Separation in
Amorphous Solid Dispersions via Raman Mapping.
Pharmaceutics 2023, 15 (5).
https://doi.org/10.3390/pharmaceutics15051395
• Janssen, L.; Sadowski, G.; Brandenbusch, C.
Continuous Phase Separation of Stable Emulsions from Biphasic
Whole-cell Biocatalysis by Catastrophic Phase Inversion.
Biotechnology journal 2023, 18 (6).
https://doi.org/10.1002/biot.202200489
• Habicht, J.; Brandenbusch, C.; Sadowski, G.
Predicting PC-SAFT Pure-Component Parameters by Machine
Learning Using a Molecular Fingerprint as Key Input.
Fluid phase equilibria 2023, 565.
https://doi.org/10.1016/j.fluid.2022.113657
• Hubach, T.; Schlüter, S.; Held, C.
Model-Based Optimization of Multi-Stage Nanofiltration Using the
Solution-Diffusion–Electromigration Model.
Processes 2023, 11 (8).
https://doi.org/10.17877/de290r-23911
• Loll, R.; Nordhausen, L.; Bieberle, A.; Schubert, M.; Pyka, T.; Koop, J.
Held, C.; Schembecker, G.
Analysis of Flow Patterns in Structured Zickzack Packings for
Rotating Packed Beds Using γ-Ray Computed Tomography.
Industrial & engineering chemistry research 2023, 62 (38), 15625–15634.
https://doi.org/10.1021/acs.iecr.3c02252
• Gajardo-Parra, N. F.; Rodríguez, G.; Arroyo-Avirama, A. F.; Veliju, A.;
Happe, T.; Canales, R. I.; Sadowski, G.; Held, C.
Impact of Deep Eutectic Solvents on Kinetics and Folding Stability of
Formate Dehydrogenase.
Processes 2023, 11 (10).
https://doi.org/10.3390/pr11102815
• Hubach, T.; Pillath, M.; Knaup, C.; Schlüter, S.; Held, C.
Li+ Separation from Multi-Ionic Mixtures by Nanofiltration
Membranes: Experiments and Modeling.
Modelling 2023, 4 (3), 408–425.
https://doi.org/10.3390/modelling4030024
• Fischer, F.; Peveling, S.; Kühl, H.-D.
Simulation and Stability Analysis of a Thermocompressor Cascade
with Overdriven Free Displacers.
Thermal science and engineering progress 2023, 44.
https://doi.org/10.1016/j.tsep.2023.102037
• Zäh, M.; Brandenbusch, C.; Winter, G.; Sadowski, G.
Predicting the Amorphous-Phase Composition during Lyophilization.
International journal of pharmaceutics 2023, 636.
https://doi.org/10.1016/j.ijpharm.2023.122836
• Ostermeier, L.; Ascani, M.; Gajardo Parra, N. F.; Sadowski, G.; Held, C.; Winter, R.
Leveraging Liquid-Liquid Phase Separation and Volume Modulation to
Regulate the Enzymatic Activity of Formate Dehydrogenase.
Biophysical chemistry 2023, 304.
https://doi.org/10.1016/j.bpc.2023.107128
• Held, C.; Liang, X.
100 Years from the Debye-Hückel Theory and Beyond.
Fluid phase equilibria; Elsevier: Amsterdam, 2023; Vol. 575.
https://doi.org/10.1016/j.fluid.2023.113931
• Aravena, P.; Cea-Klapp, E.; Gajardo Parra, N. F.; Held, C.; Garrido, J. M.;
Canales, R. I.
Effect of Water and Hydrogen Bond Acceptor on the Density and
Viscosity of Glycol-Based Eutectic Solvents.
Journal of molecular liquids 2023, 389.
https://doi.org/10.1016/j.molliq.2023.122856
SCIENTIFIC HIGHLIGHTS 2023
• Pyka, T.; Ressemann, A.; Held, C.; Schembecker, G.; Repke, J.-U.
Impact of Vapor Bypasses on Separation Performance of Rotating
Packed Beds in Distillation.
Industrial & engineering chemistry research 2023, 62 (33),
13274–13279.
https://doi.org/10.1021/acs.iecr.3c01947
• Meneses, L.; Gajardo Parra, N. F.; Cea-Klapp, E.; Garrido, J. M.; Held, C.;
Duarte, A. R.; Paiva, A.
Improving the Activity of Horseradish Peroxidase in Betaine-Based
Natural Deep Eutectic Systems.
RSC sustainability 2023, 1 (4), 886–897.
https://doi.org/10.1039/d2su00127f
• Arroyo-Avirama, A. F.; Carreño-Guzmán, S.; Lorenzo-Llanes, J.; Gajardo
Parra, N. F.; Santiago, R.; Held, C.; Palomar, J.; Canales, R. I.
In Situ Product Recovery of β-Ionone from a Fermentation Broth:
Computational Solvent Selection and Process Design of Its
Extraction and Purification.
ACS sustainable chemistry & engineering 2023, 11 (24), 9065–9076.
https://doi.org/10.1021/acssuschemeng.3c01739
• Martinez, F.; Held, C.; Siepmann, J. I.
Introducing JCED Associate Editor Fleming Martinez and Topic Editor
Christoph Held - Some Remarks on Reporting on the Solubility of
Organic Compounds and of Electrolytes.
Journal of chemical & engineering data; ACS Publ.: Washington, DC,
2023; 68, 1265–1266.
https://doi.org/10.1021/acs.jced.3c00278
• Schick, D.; Arrad, M.; Sadowski, G.; Figiel, P.; Held, C.
Modeling the Temperature-Dependent Solubility of Salts in Organic
Solvents.
Fluid phase equilibria 2023, 572.
https://doi.org/10.1016/j.fluid.2023.113828
• Pyka, T.; Brunert, M.; Koop, J.; Bieberle, A.; Held, C.; Schembecker, G.
Novel Liquid Distributor Concept for Rotating Packed Beds.
Industrial & engineering chemistry research 2023, 62 (14), 5984–5994.
https://doi.org/10.1021/acs.iecr.3c00248
• Schick, D.; Bierhaus, L.; Strangmann, A.; Figiel, P.; Sadowski, G.; Held, C.
Predicting CO2 Solubility in Aqueous and Organic Electrolyte
Solutions with EPC-SAFT Advanced.
Fluid phase equilibria 2023, 567.
https://doi.org/10.1016/j.fluid.2022.113714
• Delgado, J.; Vásquez Salcedo, W. N.; Devouge-Boyer, C.; Hebert, J.-P.;
Legros, J.; Renou, B.; Held, C.; Grenman, H.; Leveneur, S.
Reaction Enthalpies for the Hydrogenation of Alkyl Levulinates and
Levulinic Acid on Ru/C– Influence of Experimental Conditions and
Alkyl Chain Length.
Process safety and environmental protection 2023, 171, 289–298.
https://doi.org/10.1016/j.psep.2023.01.025
• Espinoza-Cartagena, F.; Ormazábal-Latorre, S.; Pazo-Carballo, C.;
Gajardo Parra, N. F.; Núñez, G. A.; Garrido, J. M.; Cea-Klapp, E.; Santiago,
R.; Held, C.; Canales, R. I.
Separation of Isoeugenol from Methylcyclohexane as a Model
Mixture of Biojet Fuel Purification: Solvent Selection and Liquid–
Liquid Equilibrium.
Industrial & engineering chemistry research 2023, 62 (30), 12006–12020.
https://doi.org/10.1021/acs.iecr.3c01440
• Koop, J.; Bera, N.; Quickert, E.; Schmitt, M.; Schlüter, M.; Held, C.;
Schembecker, G.
Separation of Volatile Organic Compounds from Viscous Liquids with
RPB Technology.
Industrial & engineering chemistry research 2023, 62 (334), 13637–13645.
https://doi.org/10.1021/acs.iecr.3c01597
Page 95
• Cea-Klapp, E.; Arroyo-Avirama, A. F.; Ormazábal-Latorre, S.; GajardoParra, N. F.; Gajardo Parra, N. F.; Pazo-Carballo, C.; Quinteros-Lama, H.;
Marzialetti, T.; Held, C.; Canales, R. I.; Garrido, J. M.
Separation of Furfuryl Alcohol from Water Using Hydrophobic Deep
Eutectic Solvents.
Journal of molecular liquids 2023, 384.
https://doi.org/10.1016/j.molliq.2023.122232
• Tsurko, E. N.; Held, C.; Kunz, W.
Thermodynamic Modeling of Aqueous Guanidinium Chloride/Sodium
l-Aspartate (Na-l-Asp) Mixtures.
Journal of solution chemistry 2023, 52 (10), 1157–1175.
https://doi.org/10.1007/s10953-023-01306-y
• Chen, Q.; Weng, J.; Sadowski, G.; Ji, Y.
Influence Mechanism of Polymeric Excipients on Drug Crystallization:
Experimental Investigation and Chemical Potential Gradient Model
Analysis and Prediction.
Crystal growth & design 2023, 23 (5), 3862–3872.
https://doi.org/10.1021/acs.cgd.3c00314
• Ge, K.; Paus, R.; Penner, V.; Sadowski, G.; Ji, Y.
A Novel Theoretical Strategy for Predicting Dissolution Kinetics and
Mechanisms of Pharmaceuticals in Complex Biorelevant Media.
International journal of pharmaceutics 2023, 648.
https://doi.org/10.1016/j.ijpharm.2023.123594
• Wolbert, F.; Luebbert, C.; Sadowski, G.
The Shelf Life of ASDs: 2. Predicting the Shelf Life at Storage
Conditions.
International journal of pharmaceutics: X 2023, 6.
https://doi.org/10.1016/j.ijpx.2023.100207
• Kloc, A. P.; Danzer, A.; Sadowski, G.
Solubility of Naproxen and Indomethacin in Supercritical Carbon
Dioxide/Ethyl Acetate Mixtures.
The journal of supercritical fluids 2023, 200.
https://doi.org/10.1016/j.supflu.2023.105990
• Pyka, T.; Backhaus, V.; Held, C.; Schembecker, G.
Impact of Number of Rotors in Rotating Packed Beds on Separation
Performance in Distillation.
Industrial & engineering chemistry research 2023, 62 (46), 19855–19861.
https://doi.org/10.1021/acs.iecr.3c03173
• Lingen, T. van; Bragoni, V.; Dyga, M.; Exner, B.; Schick, D.; Held, C.;
Sadowski, G.; Gooßen, L. J.
Salzabfall-freie Carboxylierung von Acetylen: grüne Synthese von
C4-Chemikalien durch einen CO2-Druck-induzierten Aciditätsswitch.
Angewandte Chemie 2023, 135 (27).
https://doi.org/10.1002/ange.202303882
SCIENTIFIC HIGHLIGHTS 2023
Page 96
2022
• Sauer, J.; Kühl, H.-D.
Performance Improvements in Stirling Cycle Machines by a Modified
Appendix Gap Geometry.
International journal of energy research 2022, 46 (2), 1180–1197.
https://doi.org/10.1002/er.7237
• Kroll, P.; Sadowski, G.; Brandenbusch, C.
Solubilization of Aldehydes and Amines in Aqueous CiEj Surfactant
Aggregates: Solubilization Capacity and Aggregate Properties.
Langmuir 2022, 38 (32), 10022–10031.
https://doi.org/10.1021/acs.langmuir.2c01463
• Wolbert, F.; Fahrig, I.-K.; Gottschalk, T.; Lübbert, C.; Thommes, M.;
Sadowski, G.
Factors Influencing the Crystallization-Onset Time of Metastable ASDs.
Pharmaceutics 2022, 14 (2).
https://doi.org/10.3390/pharmaceutics14020269
• Wolbert, F.; Nikoleit, K.; Steinbrink, M.; Lübbert, C.; Sadowski, G.
The Shelf Life of ASDs: 1. Measuring the Crystallization Kinetics at
Humid Conditions.
Molecular pharmaceutics 2022, 19 (7), 2483–2494.
https://doi.org/10.1021/acs.molpharmaceut.2c00188
• Chua, Y. Z.; Do, H. T. J.; Kumar, A.; Hallermann, M.; Zaitsau,
D.; Schick, C.; Held, C.
The Melting Properties of D-α-Glucose, D-β-Fructose, D-Sucrose,
D-α-Galactose, and D-α-Xylose and Their Solubility in Water: A
Revision.
Food biophysics 2022, 17 (2), 181–197.
https://doi.org/10.1007/s11483-021-09707-6
• Borrmann, D.; Danzer, A.; Sadowski, G.
Predicting the Water Sorption in ASDs.
Pharmaceutics 2022, 14 (6).
https://doi.org/10.3390/pharmaceutics14061181
• Borrmann, D.; Danzer, A.; Sadowski, G.
Water Sorption in Glassy Polyvinylpyrrolidone-Based Polymers.
Membranes 2022, 12 (4).
https://doi.org/10.3390/membranes12040434
• Borrmann, D.; Danzer, A.; Sadowski, G.
Measuring and Modeling Water Sorption in Amorphous Indomethacin
and Ritonavir.
Molecular pharmaceutics 2022, 19 (3), 998–1007.
https://doi.org/10.1021/acs.molpharmaceut.1c00984
• Huxoll, F.; Kampwerth, A.; Seidensticker, T.; Vogt, D.; Sadowski, G.
Predicting Solvent Effects on Homogeneity and Kinetics of the
Hydroaminomethylation: A Thermodynamic Approach Using PC-SAFT.
Industrial & engineering chemistry research 2022, 61 (5), 2323–2332.
https://doi.org/10.1021/acs.iecr.1c03891
• Siepmann, J. I.; Gardas, R.; Kofke, D. A.; Nieto de Castro, C.; Paulechka, E.;
Pini, R.; Sadowski, G.; Schwarz, C. E.
The Journal of Chemical & Engineering Data: Introduction of
Topical Sections and Updates from the Editorial Team.
Journal of chemical & engineering data 2022, 67 (1), 1–2.
https://doi.org/10.1021/acs.jced.1c00969
• Kroll, P.; Benke, J.; Enders, S.; Brandenbusch, C.; Sadowski, G.
Influence of Temperature and Concentration on the Self-Assembly of
Nonionic CiEj Surfactants: A Light Scattering Study.
ACS omega 2022, 7 (8), 7057–7065.
https://doi.org/10.1021/acsomega.1c06766
• Gajardo-Parra, N. F.; Akrofi-Mantey, H.; Ascani, M.; Cea-Klapp, E.; Garrido,
J. M.; Sadowski, G.; Held, C.
Osmolyte Effect on Enzymatic Stability and Reaction Equilibrium of
Formate Dehydrogenase.
Physical chemistry, chemical physics 2022, 24 (45), 27930–27939.
https://doi.org/10.1039/d2cp04011e
• Ascani, M.; Sadowski, G.; Held, C.
Calculation of Multiphase Equilibria Containing Mixed Solvents and
Mixed Electrolytes: General Formulation and Case Studies.
Journal of chemical & engineering data 2022, 67 (8), 1972–1984.
https://doi.org/10.1021/acs.jced.1c00866
• Loll, R.; Runge, L.; Koop, J.; Held, C.; Schembecker, G.
Zickzack Packings for Deaeration in Rotating Packed Beds: Improved
Rotor Design to Counter Bypass Flows.
Industrial & engineering chemistry research 2022, 61 (32), 11934–11946.
https://doi.org/10.1021/acs.iecr.2c01443
• Pabsch, D.; Figiel, P.; Sadowski, G.; Held, C.
Solubility of Electrolytes in Organic Solvents: Solvent-Specific
Effects and Ion-Specific Effects.
Journal of chemical & engineering data 2022, 67 (9), 2706–2718.
https://doi.org/10.1021/acs.jced.2c00203
• Arroyo-Avirama, A. F.; Gajardo-Parra, N. F.; Espinoza-Carmona, V.;
Garrido, J. M.; Held, C.; Canales, R. I.
Solvent Selection for the Extraction of 2-Phenylethanol from
Aqueous Phases: Density and Viscosity Studies.
Journal of chemical & engineering data 2022, 67 (8), 1893–1904.
https://doi.org/10.1021/acs.jced.1c00975
• Ascani, M.; Pabsch, D.; Klinksiek, M.; Gajardo-Parra, N.; Sadowski, G.; Held, C.
Prediction of PH in Multiphase Multicomponent Systems with
EPC-SAFT Advanced.
Chemical communications 2022, 58 (60), 8436–8439.
https://doi.org/10.1039/d2cc02943j
• Krummnow, A.; Danzer, A.; Voges, K.; Dohrn, S.; Kyeremateng, S. O.;
Degenhardt, M.; Sadowski, G.
Explaining the Release Mechanism of Ritonavir/PVPVA Amorphous
Solid Dispersions.
Pharmaceutics 2022, 14 (9).
https://doi.org/10.3390/pharmaceutics14091904
• Borrmann, D.; Danzer, A.; Sadowski, G.
Anomalous Water-Sorption Kinetics in ASDs.
Pharmaceutics 2022, 14 (9).
https://doi.org/10.3390/pharmaceutics14091897
• Arroyo-Avirama, A. F.; Ormazábal-Latorre, S.; Jogi, R.; Gajardo-Parra, N.
F.; Pazo-Carballo, C.; Ascani, M.; Virtanen, P.; Garrido, J. M.; Held, C.; MäkiArvela, P.; Canales, R. I.
Improving the Separation of Guaiacol from N-Hexane by Adding
Choline Chloride to Glycol Extracting Agents.
Journal of molecular liquids 2022, 355.
https://doi.org/10.1016/j.molliq.2022.118936
• Baco, S.; Klinksiek, M.; Ismail Bedawi Zakaria, R.; Antonia GarciaHernandez, E.; Mignot, M.; Legros, J.; Held, C.; Casson Moreno, V.;
Leveneur, S.
Solvent Effect Investigation on the Acid-Catalyzed Esterification
of Levulinic Acid by Ethanol Aided by a Linear Solvation Energy
Relationship.
Chemical engineering science 2022, 260.
https://doi.org/10.1016/j.ces.2022.117928
SCIENTIFIC HIGHLIGHTS 2023
Page 97
• Cea-Klapp, E.; Gajardo-Parra, N.; Aravena, P.; Quinteros-Lama, H.; Held,
C.; Canales, R. I.; Garrido, J. M.
Interfacial Properties of Deep Eutectic Solvents by Density Gradient
Theory.
Industrial & engineering chemistry research 2022, 61 (6), 2580–2591.
https://doi.org/10.1021/acs.iecr.1c03817
• Schick, D.; Lindfeld, J.; Schwalm, J.; Strangmann, A.; Figiel, P.; Sadowski,
G.; Held, C.
Influence of Solvent and Salt on Kinetics and Equilibrium of
Esterification Reactions.
Chemical engineering science 2022, 263.
https://doi.org/10.1016/j.ces.2022.118046
• Delgado, J.; Vasquez Salcedo, W. N.; Bronzetti, G.; Casson Moreno, V.;
Mignot, M.; Legros, J.; Held, C.; Grénman, H.; Leveneur, S.
Kinetic Model Assessment for the Synthesis of γ-Valerolactone from
n-Butyl Levulinate and Levulinic Acid Hydrogenation over the Synergy
Effect of Dual Catalysts Ru/C and Amberlite IR-120.
Chemical engineering journal 2022, 430.
https://doi.org/10.1016/j.cej.2021.133053
• Keppler, M.; Moser, S.; Jessen, H. J.; Held, C.; Andexer, J. N.
Make or Break: The Thermodynamic Equilibrium of Polyphosphate
Kinase-Catalysed Reactions.
Beilstein journal of organic chemistry 2022, 18, 1278–1288.
https://doi.org/10.3762/bjoc.18.134
• Janssen, L.; Sadowski, G.; Brandenbusch, C.
Long-Term Stable Bioprocess-Derived Pickering-Type Emulsions:
Identification of Key Parameters for Emulsion Stability Based on Cell
Interaction at Interface.
Chemical engineering science 2022, 264.
https://doi.org/10.1016/j.ces.2022.118164
• Nolte, L.; Brandenbusch, C.
Monitoring and Investigating Reactive Extraction of (Di–)Carboxylic
Acids Using Online FTIR – Part II: Reaction Equilibria, Reaction
Kinetics and Competition within the Complex Formation between
Itaconic Acid and Several Amine Extractants.
Journal of molecular liquids 2022, 366.
https://doi.org/10.1016/j.molliq.2022.120223
• Stolzke, T.; Krieg, F.; Peng, T.; Zhang, H.; Häusler, O.; Brandenbusch, C.
Hydroxylpropyl-β-Cyclodextrin as Potential Excipient to Prevent
Stress-Induced Aggregation in Liquid Protein Formulations.
Molecules 2022, 27 (16).
https://doi.org/10.3390/molecules27165094
• Stolzke, T.; Brandenbusch, C.
Simplified Choice of Suitable Excipients within Biologics Formulation
Design Using Protein-Protein Interaction- and Water Activity-Maps.
European journal of pharmaceutics and biopharmaceutics 2022, 176,
153–167.
https://doi.org/10.1016/j.ejpb.2022.05.017
• Nolte, L.; Nowaczyk, M.; Brandenbusch, C.
Monitoring and Investigating Reactive Extraction of (Di–)Carboxylic
Acids Using Online FTIR – Part I: Characterization of the Complex
Formed between Itaconic Acid and Tri-n-Octylamine.
Journal of molecular liquids 2022, 352.
https://doi.org/10.1016/j.molliq.2022.118721
• Aliyeva, M.; Brandão, P.; Gomes, J. R. B.; Coutinho, J. A. P.; Held, C.;
Ferreira, O.; Pinho, S. P.
Salt Effects on the Solubility of Aromatic and Dicarboxylic Amino
Acids in Water.
The journal of chemical thermodynamics 2022, 177.
https://doi.org/10.1016/j.jct.2022.106929
• Gajardo Parra, N. F.; Meneses, L.; Duarte, A. R. C.; Paiva, A.; Held, C.
Assessing the Influence of Betaine-Based Natural Deep Eutectic
Systems on Horseradish Peroxidase.
ACS sustainable chemistry & engineering 2022, 10 (38), 12873–12881.
https://doi.org/10.1021/acssuschemeng.2c04045
• Pyka, T.; Koop, J.; Held, C.; Schembecker, G.
Dry Pressure Drop in a Two-Rotor Rotating Packed Bed.
Industrial & engineering chemistry research 2022, 61 (46), 17156–17165.
https://doi.org/10.1021/acs.iecr.2c02500
• Ge, K.; Paus, R.; Penner, V.; Sadowski, G.; Ji, Y.
Theoretical Modeling and Prediction of Biorelevant Solubility of
Poorly Soluble Pharmaceuticals.
Chemical engineering journal 2022, 444.
https://doi.org/10.1016/j.cej.2022.136678
• Schlüter, S.; Huxoll, F.; Grenningloh, K.; Sadowski, G.; Petzold, M.; Böhm,
L.; Kraume, M.; Skiborowski, M.
Unraveling the Influence of Dissolved Gases on Permeate Flux in
Organic Solvent Nanofiltration – Experimental Analysis.
Separation and purification technology 2022, 295.
https://doi.org/10.1016/j.seppur.2022.121265
• Gottschalk, T.; Grönniger, B.; Ludwig, E.; Wolbert, F.; Feuerbach, T.;
Sadowski, G.; Thommes, M.
Influence of Process Temperature and Residence Time on the
Manufacturing of Amorphous Solid Dispersions in Hot Melt Extrusion.
Pharmaceutical development and technology an official journal of the
American Association of Pharmaceutical Scientists 2022, 27 (3), 313–318.
https://doi.org/10.1080/10837450.2022.2051549
SCIENTIFIC HIGHLIGHTS 2023
Page 98
2021
• Bülow, M.; Greive, M.; Zaitsau, D. H.; Verevkin, S. P.; Held, C.
Extremely Low Vapor-pressure Data as Access to PC‐SAFT
Parameter Estimation for Ionic Liquids and Modeling of Precursor
Solubility in Ionic Liquids.
ChemistryOpen 2021, 10 (2), 216–226.
https://doi.org/10.1002/open.202000258
• Sleziona, D.; Mattusch, A.; Schaldach, G.; Ely, D. R.; Sadowski, G.;
Thommes, M.
Determination of Inherent Dissolution Performance of Drug
Substances.
Pharmaceutics 2021, 13 (2), 146.
https://doi.org/10.17877/de290r-21914
• Greinert, T.; Vogel, K.; Maskow, T.; Held, C.
New Thermodynamic Activity-Based Approach Allows Predicting the
Feasibility of Glycolysis.
Scientific reports 2021, 11.
https://doi.org/10.1038/s41598-021-85594-8
• Ascani, M.; Held, C.
Prediction of Salting-out in Liquid-Liquid Two-Phase Systems
with EPC-SAFT: Effect of the Born Term and of a ConcentrationDependent Dielectric Constant.
Zeitschrift für anorganische und allgemeine Chemie 2021, 647 (12),
1305–1314.
https://doi.org/10.1002/zaac.202100032
• Do, H. T.; Franke, P.; Volpert, S.; Klinksiek, M.; Thome, M.; Held, C.
Measurement and Modelling Solubility of Amino Acids and Peptides
in Aqueous 2-Propanol Solutions.
Physical chemistry, chemical physics 2021, 23 (18), 10852–10863.
https://doi.org/10.1039/d1cp00005e
• Huxoll, F.; Jameel, F.; Bianga, J.; Seidensticker, T.; Stein, M.; Sadowski, G.;
Vogt, D.
Solvent Selection in Homogeneous Catalysis - Optimization of
Kinetics and Reaction Performance.
ACS catalysis 2021, 11 (2), 590–594.
https://doi.org/10.1021/acscatal.0c04431
• Jaworek, M.; Gajardo-Parra, N. F.; Sadowski, G.; Winter, R.; Held, C.
Boosting the Kinetic Efficiency of Formate Dehydrogenase by
Combining the Effects of Temperature, High Pressure and Co-Solvent
Mixtures.
Colloids and surfaces / B B, Biointerfaces 2021, 208.
https://doi.org/10.1016/j.colsurfb.2021.112127
• Gajardo-Parra, N. F.; Do, H. T. J.; Yang, M.; Pérez-Correa, J. R.; Garrido, J.
M.; Sadowski, G.; Held, C.; Canales, R. I.
Impact of Deep Eutectic Solvents and Their Constituents on the
Aqueous Solubility of Phloroglucinol Dihydrate.
Journal of molecular liquids 2021, 344.
https://doi.org/10.1016/j.molliq.2021.117932
• Huxoll, F.; Schlüter, S.; Budde, R.; Skiborowski, M.; Petzold, M.; Böhm, L.;
Kraume, M.; Sadowski, G.
Phase Equilibria for the Hydroaminomethylation of 1-Decene.
Journal of chemical & engineering data 2021, 66 (12), 4484–4495.
https://doi.org/10.1021/acs.jced.1c00561
• Borrmann, D.; Danzer, A.; Sadowski, G.
Generalized Diffusion–Relaxation Model for Solvent Sorption in
Polymers.
Industrial & engineering chemistry research 2021, 60 (43), 15766–15781.
https://doi.org/10.1021/acs.iecr.1c02359
• Veith, H.; Lübbert, C.; Rodríguez-Hornedo, N.; Sadowski, G.
Co-Crystal Screening by Vapor Sorption of Organic Solvents.
Crystal growth & design 2021, 21 (8), 4445–4455.
https://doi.org/10.1021/acs.cgd.1c00355
• Huxoll, F.; Heyng, M.; Andreeva, I. V.; Verevkin, S. P.; Sadowski, G.
Thermodynamic Properties of Biogenic Amines and Their Solutions.
Journal of chemical & engineering data 2021, 66 (7), 2822–2831.
https://doi.org/10.1021/acs.jced.1c00202
• Jastram, A.; Lindner, T.; Lübbert, C.; Sadowski, G.; Kragl, U.
Swelling and Diffusion in Polymerized Ionic Liquids-Based Hydrogels.
Polymers 2021, 13 (11).
https://doi.org/10.3390/polym13111834
• Veith, H.; Lübbert, C.; Sadowski, G.
Predicting Deliquescence Relative Humidities of Crystals and Crystal
Mixtures.
Molecules 2021, 26 (11).
https://doi.org/10.3390/molecules26113176
• Bülow, M. R.; Gerek Ince, N.; Hirohama, S.; Sadowski, G.; Held, C.
Predicting Vapor–Liquid Equilibria for Sour-Gas Absorption in
Aqueous Mixtures of Chemical and Physical Solvents or Ionic Liquids
with EPC-SAFT.
Industrial & engineering chemistry research 2021, 60 (17), 6327–6336.
https://doi.org/10.1021/acs.iecr.1c00176
• Gardas, R. L.; Kofke, D. A.; Pini, R.; Sadowski, G.; Schwarz, C. E.;
Siepmann, J. I.; Wu, J.
Historical Perspective of the Journal of Chemical & Engineering
Data’s Published Topics, 1956–2020.
Journal of chemical & engineering data 2021, 66 (4), 1555–1556.
https://doi.org/10.1021/acs.jced.1c00193
• Brinkmann, J.; Exner, L.; Verevkin, S. P.; Lübbert, C.; Sadowski, G.
PC-SAFT Modeling of Phase Equilibria Relevant for Lipid-Based Drug
Delivery Systems.
Journal of chemical & engineering data 2021, 66 (3), 1280–1289.
https://doi.org/10.1021/acs.jced.0c00912
• Siepmann, J. I.; Gardas, R. L.; Kofke, D. A.; Pini, R.; Sadowski, G.; Schwarz,
C. E.; Wu, J.
Journal of Chemical & Engineering Data: Why Change the Cover
Page?
Journal of chemical & engineering data; ACS Publ.: Washington, DC,
2021; Vol. 66, pp 859–860.
https://doi.org/10.1021/acs.jced.1c00048
• Sepúlveda-Orellana, B.; Gajardo-Parra, N. F.; Do, H. T.; Pérez-Correa, J. R.;
Held, C.; Sadowski, G.; Canales, R. I.
Measurement and PC-SAFT Modeling of the Solubility of Gallic Acid
in Aqueous Mixtures of Deep Eutectic Solvents.
Journal of chemical & engineering data 2021, 66 (2), 958–967.
https://doi.org/10.1021/acs.jced.0c00784
• Sosa, A.; Ortega, J.; Fernández, L.; Haarmann, N.; Sadowski, G.
Methodology Based on the Theory of Information to Describe the
Representation Ability of the DMC + Alkane Behavior.
Industrial & engineering chemistry research 2021, 60 (2), 1036–1054.
https://doi.org/10.1021/acs.iecr.0c05301
• Siepmann, J. I.; Gardas, R. L.; Kofke, D. A.; Pini, R.; Sadowski, G.; Schwarz,
C.; Wu, J.
Journal of Chemical & Engineering Data: An Update from the
Editorial Team.
Journal of chemical & engineering data 2021, 66 (1), 1–2.
https://doi.org/10.1021/acs.jced.0c01080
SCIENTIFIC HIGHLIGHTS 2023
Page 99
• Kühl, H.-D.; Sauer, J.
Appendix Gap Losses in Stirling Engines: Review of Recent Findings.
19th International Stirling Engine Conference (ISEC 2021); EDP Sciences:
London, 2021; Vol. 313.
https://doi.org/10.1051/e3sconf/202131303001
• Sun, Y.; Zuo, Z.; Shen, G.; Held, C.; Lu, X.; Ji, X.
Modeling Interfacial Properties of Ionic Liquids with EPC-SAFT
Combined with Density Gradient Theory.
Fluid phase equilibria 2021, 536.
https://doi.org/10.1016/j.fluid.2021.112984
• Fischer, F.; Kühl, H.-D.
Generation of Compressed Air by Cascaded Thermocompressors –
Project Status.
19th International Stirling Engine Conference (ISEC 2021); EDP Sciences:
London, 2021; Vol. 313.
https://doi.org/10.1051/e3sconf/202131304003
• Do, H. T. J.; Chakrabarty, S.; Held, C.
Modeling Solubility of Amino Acids and Peptides in Water and in
Water+2-Propanol Mixtures: PC-SAFT vs. GE Models.
Fluid phase equilibria 2021, 542–543.
https://doi.org/10.1016/j.fluid.2021.113087
• Dohrn, S.; Rawal, P.; Lübbert, C.; Lehmkemper, K.; Kyeremateng, S. O.;
Degenhardt, M.; Sadowski, G.
Predicting Process Design Spaces for Spray Drying Amorphous Solid
Dispersions.
International journal of pharmaceutics: X 2021, 3.
https://doi.org/10.1016/j.ijpx.2021.100072
• Bueno, A.; Lübbert, C.; Enders, S.; Sadowski, G.; Smirnova, I.
Production of Polylactic Acid Aerogels via Phase Separation and
Supercritical CO2 Drying: Thermodynamic Analysis of the Gelation
and Drying Process.
Journal of materials science 2021, 56 (34), 18926–18945.
https://doi.org/10.1007/s10853-021-06501-0
• Ji, Y.; Hao, D.; Lübbert, C.; Sadowski, G.
Insights into Influence Mechanism of Polymeric Excipients on
Dissolution of Drug Formulations: A Molecular Interaction-based
Theoretical Model Analysis and Prediction.
AIChE journal / American Institute of Chemical Engineers 2021, 67 (11).
https://doi.org/10.1002/aic.17372
• Dohrn, S.; Lübbert, C.; Lehmkemper, K.; Kyeremateng, S. O.; Degenhardt,
M.; Sadowski, G.
Solvent Mixtures in Pharmaceutical Development: Maximizing the
API Solubility and Avoiding Phase Separation.
Fluid phase equilibria 2021, 548.
https://doi.org/10.1016/j.fluid.2021.113200
• Veith, H.; Zaeh, M.; Lübbert, C.; Rodríguez-Hornedo, N.; Sadowski, G.
Stability of Pharmaceutical Co-Crystals at Humid Conditions Can Be
Predicted.
Pharmaceutics 2021, 13 (3).
https://doi.org/10.3390/pharmaceutics13030433
• Brinkmann, J.; Becker, I.; Kroll, P.; Lübbert, C.; Sadowski, G.
Predicting the API Partitioning between Lipid-Based Drug Delivery
Systems and Water.
International Journal of Pharmaceutics 2021, 595.
https://doi.org/10.1016/j.ijpharm.2021.120266
• Prell, C.; Busche, T.; Rückert, C.; Nolte, L.; Brandenbusch, C.; Wendisch, V. F.
Adaptive Laboratory Evolution Accelerated Glutarate Production by
Corynebacterium Glutamicum.
Microbial cell factories 2021, 20.
https://doi.org/10.1186/s12934-021-01586-3
• Wessner, M.; Meier, M.; Bommarius, B.; Bommarius, A. S.; Brandenbusch, C.
Intensifying Aqueous Two-Phase Extraction by Adding Decisive
Excipients for Enhancement of Stability and Solubility of
Biomolecules.
Chemical engineering and processing 2021, 167.
https://doi.org/10.1016/j.cep.2021.108534
• Do, H. T. J.; Chua, Y. Z.; Habicht, J.; Klinksiek, M.; Volpert, S.; Hallermann,
M.; Thome, M.; Pabsch, D.; Schick, D.; Zaitsau, D.; Schick, C.; Held, C.
Melting Properties of Peptides and Their Solubility in Water. Part 2:
Di- and Tripeptides Based on Glycine, Alanine, Leucine, Proline, and
Serine.
Industrial & engineering chemistry research 2021, 60 (12), 4693–4704.
https://doi.org/10.1021/acs.iecr.0c05652
• Roda, A.; Santos, F.; Chua, Y. Z.; Kumar, A.; Do, H. T. J.; Paiva, A.; Duarte, A.
R. C.; Held, C.
Unravelling the Nature of Citric Acid:l-Arginine:Water Mixtures: The
Bifunctional Role of Water.
Physical chemistry, chemical physics 2021, 23 (2), 1706–1717.
https://doi.org/10.1039/d0cp04992a
• Bülow, M. R.; Ascani, M.; Held, C.
EPC-SAFT Advanced - Part I: Physical Meaning of Including a
Concentration-Dependent Dielectric Constant in the Born Term and
in the Debye-Hückel Theory.
Fluid phase equilibria 2021, 535.
https://doi.org/10.1016/j.fluid.2021.112967
• Bülow, M. R.; Ascani, M.; Held, C.
EPC-SAFT Advanced – Part II: Application to Salt Solubility in Ionic
and Organic Solvents and the Impact of Ion Pairing.
Fluid phase equilibria 2021, 537.
https://doi.org/10.1016/j.fluid.2021.112989
• Wysoczanska, K.; Nierhauve, B.; Sadowski, G.; Macedo, E. A.; Held, C.
Solubility of DNP-Amino Acids and Their Partitioning in
Biodegradable ATPS: Experimental and EPC-SAFT Modeling.
Fluid phase equilibria 2021, 527.
https://doi.org/10.1016/j.fluid.2020.112830
SCIENTIFIC HIGHLIGHTS 2023
Transport Processes (TP)
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SCIENTIFIC HIGHLIGHTS 2023
Page 101
Publications
2023
Publications Alba Diéguez Alonso
• A. Dieguez-Alonso, T.-L.E. Vu-Han, H. Almuina-Villar, J.J. Rico Fuentes, L.
Hilfert, A. Dernbecher, J.M. de la Rosa, F. Behrendt
Tailored production and application of biochar for tar removal
Fuel 2023, 348, 128306.
https://doi.org/10.1016/j.fuel.2023.128306
• D.D. Attanayake, F. Sewerin, S. Kulkarni, A. Dernbecher, A. DieguezAlonso, B. van Wachem
Review of modelling of pyrolysis processes with CFD-DEM
Flow, Turbulence and Combustion 2023, 111 (2), 355-408.
https://doi.org/10.1007/s10494-023-00436-z
• J.J. Rico, R. Pérez-Orozco, J. Porteiro, D. Patiño
Effect of air staging and porous inert material on the emission of
volatile organic compounds in solid biomass combustion
Fuel 2023, 351, 128907.
https://doi.org/10.1016/j.fuel.2023.128907
• G.F. García Sánchez, J.L. Chacón Velasco, D.A. Fuentes Díaz, Y.J. RuedaOrdóñez, D. Patiño, J.J. Rico, J.R. Martínez Morales
Biomass Combustion Modeling Using OpenFOAM: Development
of a Simple Computational Model and Study of the Combustion
Performance of Lippia origanoides Bagasse
Energies 2023, 16(6), 2932.
https://doi.org/10.3390/en16062932
2022
• L. Wang, M. N. Olsen, C. Moni, A. Dieguez-Alonso, J. M. de la Rosa, M.
Stenrød, X. Liu, and L. Mao.
Comparison of properties of biochar produced from different types of
lignocellulosic biomass by slow pyrolysis at 600 °C
Applications in Energy and Combustion Science 2022, 12, 100090.
https://doi.org/10.1016/j.jaecs.2022.100090
• A. Anca-Couce, L. von Berg, G. Pongratz, R. Scharler, C. Hochenauer, M.
Geusebroek, J. Kuipers, C. Mourao Vilela, T. Kraia, K. Panopoulos, I. Funcia,
A. Dieguez-Alonso, H. Almuina-Villar, T. Tsiotsias, N. Kienzl, and S. Martini.
Assessment of measurement methods to characterize the producer
gas from biomass gasification with steam in a fluidized bed
Biomass and Bioenergy 2022, 163, 106527.
https://doi.org/10.1016/j.biombioe.2022.106527
• A. Dernbecher and A. Dieguez-Alonso.
Advanced porous particle model in biomass pyrolysis
Chemical Engineering Transactions 2022, 92, 685–690, 2022.
https://doi.org/10.3303/CET2292115
• S. M. Weldon, B. van der Veen, E. Farkas, N. Kocatürk-Schumacher, A.
Dieguez-Alonso, A. Budai, and D. P. Rasse
A re-analysis of NH4+ sorption on biochar: have expectation been
been too high?
Chemosphere 2022, 301, 134662, 2022.
https://doi.org/10.1016/j.chemosphere.2022.134662
• H. Khodaei, C. Olson, D. Patiño, J.J. Rico, Q. Jin, A. Boateng
Multi-objective utilization of wood waste recycled from construction
and demolition (C&D): Products and characterization
Waste Maganement 2022, 149, 228-238.
https://doi.org/10.1016/j.wasman.2022.06.021
• J.J. Rico, R. Pérez-Orozco, D. Patiño Vilas, J. Porteiro,
TG/DSC and kinetic parametrization of the combustion of agricultural
and forestry residues
Biomass and Bioenergy 2022, 162, 106485.
https://doi.org/10.1016/j.biombioe.2022.106485
2021
• J.L. Míguez, J. Porteiro, F. Behrendt, D. Blanco, D. Patiño, and A. DieguezAlonso.
Review of the use of additives to mitigate operational problems
associated with the combustion of biomass with high content in
ash-forming species
Renewable and Sustainable Energy Reviews 2021, 141, 110502.
https://doi.org/10.1016/j.rser.2020.110502
• P. Maziarka, C. Wurzer, P. J. Arauzo, A. Dieguez-Alonso, O. Mašek, and F.
Ronsse.
Do you BET on routine? The reliability of N2 physisorption for the
quantitative assessment of biochar’s surface area
Chemical Engineering Journal 2021, 418, 129234.
https://doi.org/10.1016/j.cej.2021.129234
• A. Dernbecher and A. Dieguez-Alonso.
Advanced porous particle model in biomass pyrolysis
Chemical Engineering Transactions 2022, 92, 685–690, 2022.
https://doi.org/10.3303/CET2292115
SCIENTIFIC HIGHLIGHTS 2023
Impressum
TU Dortmund
www.bci.tu-dortmund.de
Redaktion: Prof. Joerg C. Tiller
Publication date: September 2024