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Anticancer Activity of Some Ruthenium(III) Complexes with Quinolone Antibiotics: In Vitro Cytotoxicity, Cell Cycle Modulation, and Apoptosis-Inducing Properties in LoVo Colon Cancer Cell Line
Article
Volume 6, Issue 4, 2024, 34
https://doi.org/10.33263/Materials64.034
Performance and Efficiency of Cirsium arvense Leaves
Extract (CALE) as an Eco-Friendly Inhibitor for Carbon
Steel in 1.0 M HCl
Mohammed Ellaite 1, Issam Forsal 1,*
1
*
, Sara Lahmady 1
Laboratory of Engineering and Applied Technologies, School of Technology, Beni Mellal, Morocco
Correspondence: forsalissam@yahoo.fr (F.I.);
Scopus Author ID 35434746700
Received: 27.02.2024; Accepted: 6.10.2024; Published: 10.12.2024
Abstract: Current research aims to develop non-toxic, biodegradable, and environmentally friendly
inhibitors. This study assessed the ability of Cirsium arvense leaf extract (CALE) to inhibit carbon steel
corrosion in molar hydrochloric acidic conditions. Using electrochemical impedance spectroscopy
(EIS) and potentiodynamic polarization (PDP) methods, the inhibitory effectiveness η% of (CALE) was
evaluated. The effects of inhibitor temperatures (293-323K) and concentrations (200–800 ppm) were
studied. With 600 ppm of (CALE) at 293K, the optimal η% of 94% was obtained. The Nyquist graphs
demonstrate how rising (CALE) concentration reduces double-layer capacitance and raises chargetransfer resistance due to the (CALE) molecules' adsorption on the CS surface. A mixed-type inhibitory
behavior was demonstrated via potentiodynamic polarization.
Keywords: Cirsium arvense leaves extract; corrosion; friendly inhibitors; potentiodynamic
polarization.
© 2024 by the authors. This article is an open-access article distributed under the terms and conditions of the Creative
Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/).
1. Introduction
Metal corrosion is a common occurrence during metal processing, transportation, and
storage. Consequently, acid pickling becomes essential as a preparatory step before surface
treatment, removing rust and deposited layers from the metal surface [1,2]. Strongly acidic
solutions, such as phosphoric, hydrochloric, sulfuric, and nitric acids, are widely used as
pickling solutions in the industrial sector [3-5]. As HCl can be cleaned more quickly at room
temperature and in a smaller amount than other acids, it is frequently used to cure metal
surfaces. Because it doesn't release effluents, including nitrogen and phosphorus, it is less
damaging to the environment [6,7]. On the contrary, the use of hydrochloric acid for pickling
also presents limitations due to its tendency to induce corrosion on metal surfaces [8,9].
Inhibitors are still the most efficient, popular, and cost-effective way to prevent the
deterioration of metals and alloys [10,11]. Several studies on corrosion inhibition have been
performed, including synthetic (organic and non-organic) inhibitors [12,13] and eco-friendly
inhibitors [14]. Natural materials, like extracts or essential oils, have drawn much interest lately
as low-cost, environmentally friendly corrosion inhibitors. They don't include heavy metals or
other harmful substances. Thus, their prospects for the environment are excellent [15,16]. It is
reported that the majority of these green inhibitors contain substances such as flavonoids,
alkaloids, polyphenols, and other organic compounds with heteroatoms (O, N, S), π system,
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and functional groups such as -NH-, -N=N-, -C=N-, and R-OH in their molecular structure,
which promotes their adsorption on metal surfaces and thus the formation of a film that acts as
a barrier between the metal and the corrosive medium [17–20]. According to the literature, the
performance of the adsorption process is influenced by the chemical composition of the
inhibitor, the presence of an active center, the availability of donor or repellent groups,
temperature, solution acidity, soak time, and other parameters [21,22].
This study used electrochemical methods, including electrochemical impedance (EIS)
and potentiodynamic polarization (PDP), to examine the inhibitory effect of an extract from
the leaves of Cirsium arvense on the corrosion behavior of carbon steel in a molar solution of
hydrochloric acid. The PDP technique was applied, with temperatures being changed from 293
K to 323K, To investigate how this parameter affected the performance of (CALE).
2. Materials and Methods
2.1. Materials and electrolyte preparation.
Carbon steel (CS) specimens with the following composition (weight %): 0.07 C, 0.19
Mn, 0.03 Si, 0.05 Cr, 0.02 Al, and balance Fe were used in this investigation. Before each
electrochemical experiment, the CS electrode was carefully polished with emery papers with
different degrees of roughness from Nº 220 to N° 2000. The polished electrode was rinsed with
distilled water, degreased with acetone, and dried with warm air before use. The electrolyte of
this work is a solution prepared from 37% HCl of the brand LOBA Chemie, and it was used to
prepare acidic media at a concentration of 1.0 mol/L by diluting it with distilled water.
2.2. Inhibitor (CALE) preparation.
The Cirsium arvense leaves were harvested in Morocco's Marrakech region. The fresh
leaves were washed to remove dust before drying in the shade for 15 days at room temperature
(25°C-27°C). A blender was used to crush the dried material into powder. The extraction was
carried out using maceration in ethanol. The powdered sample (25 g) was stirred in 200 mL of
ethanol for 48 hours at room temperature while protected from light. At 45°C, a rotary
evaporator concentrated the filtered product.
2.3. Electrochemical measurements.
Utilizing electrochemical techniques, the processes and phenomena involved in the
corrosion of carbon steel in HCl 1M have been investigated. All electrochemical studies were
carried out with a potentiostat of the type OrigaStat 100, which was controlled by the
Origamaster5 software. The cell was equipped with three electrodes: a carbon steel working
electrode, a platinum counter electrode, and a saturated calomel electrode (SCE) as a reference
electrode. A surface area of 0.64 cm² of the working electrode was exposed to the electrolyte.
By submerging the working electrode in the corrosive medium for 30 minutes with and without
(CALE), open circuit potential (OCP) surveillance was carried out.
Using a scan rate of 1 mV/s, the potential was changed from -750 to -100 mV (vs. SCE)
to execute the potentiodynamic polarization curves on the carbon steel electrode. The
polarization curve test's accompanying electrochemical data, including corrosion current
density (icorr), corrosion potential (Ecorr), anode Tafel slope (βa), and cathode Tafel slope
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(βc), can be obtained using linear extrapolation. The following equation can be used to
determine the corrosion inhibition efficiency (η%) of the polarization curve test [23]:
(η%) =
Icorr −I′ corr
Icorr
∗ 100
(1)
where Icorr and I'corr denote the corrosion current densities, respectively, in the
presence and absence of CALE.
Electrochemical impedance spectroscopy investigations were conducted by applying a
signal amplitude perturbation of 10 mV in the frequency range of 1 KHz to 100 MHz. Using
EC-LAB software, the impedance data were assessed, and the findings were typically fitted to
a suitable equivalent electrical circuit. Using the following formula, the inhibitory efficiency
was determined [24]:
(η%) =
Rct − Rct0
Rct
∗ 100
(2)
The charge transfer resistance values in the presence and absence of CALE are denoted
by R ct0 and R ct , respectively.
3. Results and Discussion
3.1. Potentiodynamic polarization curves.
To understand the dynamics of metal corrosion and the impact of extract from Cirsium
arvense leaves on the corrosion kinetics of carbon steel dissolving, this section of the research
attempts to provide some clarification. At 293K and 1.0 mol/L HCl concentration, the
polarization curves of the CS electrode are displayed in Figure 1, both with and without varying
CALE concentrations. Table 1 lists the corrosion parameters combined with the inhibitor's
inhibition efficacy that is being studied.
Logi(mA/cm²)
2
0
-2
Blank
200 ppm
400 ppm
600 ppm
800 ppm
-4
-6
-0,7
-0,6
-0,5
-0,4
-0,3
-0,2
-0,1
E(V/SCE)
Figure 1. Potentiodynamic polarization curves of CS corrosion in the absence and presence of various
concentrations of CALE.
Table 1. Polarization parameters of CS in 1 M HCl solution without and with different concentrations of CALE
at 293K.
Concentration
ppm
Blank
200
400
600
800
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Icorr
(µA/cm2)
322.8
27.9
25.3
19.2
23.0
-Ecorr
(mV vs SCE)
536.0
473.3
487.9
489.9
472.9
βa
(mV/dec)
99.4
67.5
81.0
81.5
69.2
-βc
(mV/dec)
117.7
130.8
123.5
146.7
147.6
𝛈%
91
92
94
93
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The study's findings (Figure 1) demonstrate that the corrosion potential values shifted
in the anodic direction for all CALE inhibitor doses. The literature states that an inhibitor can
be categorized as anodic or cathodic if the displacement of Ecorr of inhibited solutions relative
to the blank solution is larger than 85 mV and that the inhibitor's mixed nature can account for
Ecorr shifts of less than 85 mV [25]. In this investigation, we discovered that the displacement
was less than 85 mV and the corrosion potential values did not differ considerably, suggesting
that CALE acted as mixed-type inhibitors. Table 1 shows that as CALE concentration rises, a
significant decrease in corrosion current density (icorr) results in an increase in inhibition
efficiency, which reaches its maximum value (94%) at 600 ppm.
3.2. Electrochemical impedance spectroscopy (EIS).
An effective method for evaluating the adsorption process, electrode kinetics, and
surface characteristics is electrochemical impedance spectroscopy (EIS) [26]. EIS
measurements were performed in HCl 1M, both with and without varying inhibitor quantities.
The CS's Nyquist spectra are displayed in Figure 2. Table 2 is a summary of the values derived
from Figure, which include the exponential value of CPE (n), η%, double layer capacitance
(Cdl), constant phase element (Qdl), electrolyte resistance (Rs), and charge transfer resistance
(Rct).
1000
Blank
200 ppm
400 ppm
600 ppm
800 ppm
Fitting
-Zim (Ω.cm2 )
800
600
400
200
0
0
200
400
600
800
1000
1200
1400
Zre (Ω.cm2 )
Figure 2. Nyquist plots for CS corrosion in 1.0 M HCl with different concentrations of CALE at 293K.
Figure 2 analysis reveals that all impedance graphs exhibit capacitive loops,
demonstrating that charge transfer regulates steel corrosion [27]. The corrosion mechanism of
CS remains unaffected by the presence of extract from Cirsium arvense leaves. Semicircles'
diameters are significantly altered when this inhibitor is added to a corrosive environment; their
diameters rise with CALE concentration. The non-perfect capacitive loops in Nyquist plots can
be attributed to the inhomogeneities of carbon steel and frequency dispersion [28,29].
Table 2's research demonstrates that while the double-layer capacitance decreases with
increasing inhibitor concentration, the charge transfer resistance increases. A drop in the local
dielectric constant and/or an increase in the electrical double layer's thickness increases Rct,
suggesting a protective layer on the CS surface [30,31].
Table 2 shows that when the amount of Cirsium arvense leaves increases, the corrosion
inhibition efficiency increases as well, suggesting that the film formed by CALE molecules on
the CS surface gets denser and more organized [32]. The percentage can reach 93% when the
CALE extract content reaches 600 ppm.
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Table 2. Impedance parameters of CS in acidic medium in uninhibited and inhibited medium at 293K.
Concentration
(ppm)
Blank
200
400
600
800
Rs
(Ω.cm2)
0.62
1.17
1.33
0.63
1.24
Rct
(Ω.cm2)
87.78
681.2
790.9
1284
1029
Cdl
(μF.cm-2)
211.3
89.34
61.86
38.23
55.74
n
0.88
0.89
0.89
0.89
0.89
Qdl
(μΩ−1 cm−2 Sn)
340
118.3
88.3
63.4
82.4
η%
87
89
93
91
3.3. Effect of temperature on corrosion inhibition.
Through potentiodynamic polarization, the influence of temperature on the inhibition
efficiency of carbon steel in 1M HCl containing 600 ppm of CALE was determined at
temperatures ranging from 293K to 323K and in the absence of an inhibitor (Figure 3).
Figure 3. Potentiodynamic polarization curves of CS in the HCl 1M and in HCl 1M + 600 ppm of CALE at different ranges
of temperature.
The optimal inhibitor concentration, corresponding to the highest percentage, was
determined to be 600 ppm. The corresponding data are displayed in Table 3.
Table 3. Electrochemical parameters of CS in the HCl 1M and in HCl 1M + 600 ppm of CAVE in at different
ranges of temperature.
Blank
600 ppm of
CALE
T (K)
293
303
313
323
293
303
313
323
Icorr(µA/cm2)
322.8
417.6
557.7
1419.0
19.2
36.5
38.6
62.3
-Ecorr(mV vs SCE)
536.0
494.7
494.4
476.5
489.9
491.5
473.9
466.0
βa (mV/dec)
99.4
106.0
121.3
113.7
81.5
77.2
67.1
50.3
-βc (mV/dec)
117.7
132.9
145.3
160.4
146.7
155.3
138.0
211.5
η%
94
91
93
95
It is evident that increasing the temperature increases the cathodic and anodic currents
of the CS electrode both in the presence and absence of CALE. Table 3 shows that the inhibition
effectiveness (η%) increases as the temperature rises, suggesting that CALE functions well as
an inhibitor at high temperatures. Its inhibitory efficiency has thereby grown (from 94% to
95%). This indicates that the inhibitor molecules are more likely to adsorb onto the metal
surface and block the active corrosion sites [33].
4. Conclusions
The findings of this study demonstrate that Cirsium arvense leaf extract (CALE)
functions as a potent inhibitor against carbon steel corrosion in 1M HCl. The protective
effectiveness of CALE was found to increase with higher concentrations, reaching maximum
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efficiencies of approximately 94% at 600 ppm and 293K. Moreover, the inhibitory properties
of CALE were assessed across a temperature range of 293 K to 323 K. Analysis of the
potentiodynamic polarization (PDP) results indicated that CALE acts as a mixed-type inhibitor
with a pronounced anodic character. Additionally, the electrochemical impedance
spectroscopy (EIS) data corroborated well with the findings from the PDP experiments.
Funding
This research received no external funding.
Acknowledgments
We thank all our colleagues.
Conflicts of Interest
The authors declare no conflict of interest.
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