17-JMES,绿色化学缓蚀剂英文文献.doc

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1、17-JMES,绿色化学缓蚀剂英文文献 J. Mater. Environ. Sci. 4 (1) (2021) 127-138 Benali et al. ISSN : 2028-2508 CODEN: JMESCN Green corrosion inhibitor: inhibitive action of tannin extract of Chamaerops humilis plant for the corrosion of mild steel in 0.5 M H2SO4 Department of Biology, Faculty of Sciences and Techn

2、ology ,Univesrity Dr Moulay Tahar - Sa?da (Algeria) 2 Department of Engineering Procedures, University of Bechar 08000 Algeria. 3Laboratory of LASNABIO, Department of Chemistry, University of Tlemcen 13000 Algeria. 4Equipe de Gnie de lEnvironnement et de Biotechnologie, ENSA, Universit Ibn Zohr, BP

3、1136 Agadir, Morocco 1O. Benali *, H. Benmehdi , O. Hasnaoui 1, C. Selles 3, R. Salghi4 1,2 Received 08 Aug 2021, Revised 11 Sept 2021, Accepted 11 Sept 2021 *Corresponding author. Email: Abstract The corrosion and inhibition behaviors of mild steel in sulfuric acid + 5% EtOH in the presence of tann

4、in extract of Chamaerops humilis plant (LF-Ch) and potassium iodide (KI) have been studied using the electrochemical methods. It was found that the inhibition efficiency increased with LF-Ch extract concentration. The addition of potassium iodide to LF-Ch extract in solution increased the inhibition

5、 efficiency of this latter. A synergistic effect was observed between KI and extract with optimum of concentration of 100 mg /L LF-Ch extract + 0.025% potassium iodide. Adsorption of extract alone or in combination with potassium iodide on the metal surface obeyed the Langmuir adsorption isotherm an

6、d thermodynamic calculations revealed that the adsorption of inhibitor were of chemical nature. That suggest the presence of iodide ions in solution increases the surface coverage. The adsorption of LF-Ch extract on the mild steel in aggressive medium leads to the formation of a protective film whic

7、h grows in thickness and effectiveness with increasing exposure time. Keywords: Mild steel, corrosion test, electromechanical techniques, adsorption, synergistic effect. 1. Introduction Corrosion problems in the oil and petrochemical industry usually have been solved by the selection of suitable mat

8、erials and/or by changing the environment to make it less aggressive 1. Acid solutions are widely used in the industry. The most important areas of application are acid pickling, industrial acid cleaning, acid descaling and oil well acidizing 2. Corrosion inhibitors are needed to reduce the corrosio

9、n rates of metallic materials in these acid media 3-8. An inhibitor is usually added in small amount in order to slow down the rate of corrosion through the mechanism of adsorption 9-10. Over the years, several inhibitors have been synthesised or chosen from existing compounds and it has been found

10、that the best inhibitors are those that have centre for electron donation (usually enhanced by the presence of hetero atoms in aromatic compound) while others may be gotten from extracts of naturally occurring compounds 11-13. The last class of inhibitors (green inhibitors) are significant because t

11、hey are non toxic and do not contain heavy metals hence they are environmentally friendly 14-15. The present study is aimed at investigating the inhibitive and adsorption properties of tannin extract of Chamaerops humilis (LF-Ch) for the corrosion of mild steel in H2SO4. 127 J. Mater. Environ. Sci.

12、4 (1) (2021) 127-138 Benali et al. ISSN : 2028-2508 CODEN: JMESCN 2. Experimental 2. 1. Plant Material The leaves and fruits pericarp of the Chamaerops humilis (LF-Ch) plant were collected from mountains located at western Algeria (Tlemcen area) in july 2021. From a geographical point of view, the d

13、istricts are located, respectively in the mountains of Trara (3 districts: Djebala, Fillaoucene, Ronaine) and in the mounts of Tlemcen (2 districts: Oued Chouly (currently Oued Lakhdar) and Azails). The plant sample was identified by the authors. The voucher specimen was deposited in the Biological

14、Science laboratory of the ecology, Department of Biology - University Abou Bakr Belkaid of Tlemcen. The plant organs were cut into small pieces and shade dried at room temperature (20C) for two weeks, finely powdered plant materials were stored in airtight polythene bags protected from sunlight unti

15、l use. 2. 2. Preparation of the tannins extract A total of 425 g of defatted powder of each parts (leaves or pericarp fruit) were contacted with 1700 mL of acetone/water (70:30, v/v) in 2000 mL capped flask with timely shaking and stirring for 4 days at ambient temperature (maceration). The obtained

16、 extract was filtered by using Whatmann filter paper and then acetone was removed from the extract by using a rotary evaporator. The aqueous extract was extracted respectively with dichloromethane (2x100 mL) and 4x100 mL with diethyl acetate. The organic layer (AcOEt) was dried with Na2SO4, filtered

17、 and concentrated to dryness to give crude extract of tannins as a brownish solid (m=1,9g; yield=0,446%; mp=110-120C) 16. The Phytochemical investigation of leaves and fruits extracts of this plant was done in detail in our previous work 17. 2. 3. Solution and material A 0.5 M H2SO4 solution was pre

18、pared from an analytical reagent grade of H2SO4 98% and distilled water + 5% of Ethanol absolute and was used as corrosion media in the studies. For the electrochemical measurements, the experiments were carried out in solution of 0.5 M sulfuric acid +5 % Ethanol (uninhibited and inhibited) on mild

19、steel of composition (wt%) : C 0.1%, Si 0.03%, Mn 0.2%, P 0.02%, Cr 0.05%, Ni 0.05%, Al 0.03% and the remainder iron. Specimens in the form of disc were abraded successively with different grades of emery paper up 1200 grade. 2. 4. Electrochemical measurements Electrochemical experiments were carrie

20、d out in a glass cell (CEC/TH-Radiometer) with a capacity of 500 mL. A platinum electrode (1cm2) and a saturated calomel electrode (SCE) were used as a counter electrode and a reference electrode, respectively. The working electrode (WE) was in the form of a disc cut from mild steel under investigat

21、ion and was embedded in a Teflon rod with an exposed area of 0.5 cm2. Electrochemical impedance spectroscopy (EIS), potentiodynamic and linear polarization were conducted in an electrochemical measurement system (VoltaLab40) which comprises a PGZ301 potentiostat, a personal computer and VoltaMaster

22、4 and Zview software. The potentiodynamic currentpotential curves were recorded by changing the electrode potential automatically from 800 to 200 mV with scanning rate of 2 mV s1. The polarization resistance measurements were performed by applying a controlled potential scan over a small range typic

23、ally 10 mV with respect to Ecorr. The resulting current is linearly plotted against potential, the slope of this plot at Ecorr being the polarization resistance (Rp). All experiments were carried out in freshly prepared solution at constant temperature 32 0.1 C using a thermostat. The ac impedance m

24、easurements were performed at corrosion potentials (Ecorr) over a frequency range of 10 kHz 100 mHz, with a signal amplitude perturbation of 10 mV. Nyquist plots were obtained. 128 J. Mater. Environ. Sci. 4 (1) (2021) 127-138 Benali et al. ISSN : 2028-2508 CODEN: JMESCN From the measured polarizatio

25、n resistance value, the inhibition efficiency has been calculated using the relationship: R0pIERp(%)=1?100 (1) Rip where R0p and Rip are the polarization resistance in absence and in presence of inhibitor, respectively. The inhibition efficiency was evaluated from the measured Icorr values using the

26、 relationship: iIEIcorr(%)=1?icorr100 (2) i0corr where i0corr and iicorr are the corrosion current density in absence and in presence of inhibitor, respectively. The inhibition efficiency was evaluated from the calculated Corrosion rate (C.R) using the relationship: C.RIEC.R(%)=1?100 (3) C.R0 where

27、C.R0 and C.R are the corrosion rate in absence and in presence of inhibitor, respectively. The inhibition efficiency of the inhibitor has been found out from the charge transfer resistance values using the following equation: R IERt(%)=1?0t100 (4) Rit where R0t and Rit are the charge transfer resist

28、ance in absence and in presence of inhibitor, respectively. 3. Results and discussion 3. 1. Polarization measurements Potentiodynamic anodic and cathodic polarization scans were carried out at 320.1 C in 0.5 M H2SO4 +5% EtOH with different concentrations of LF-Ch extract. Anodic and cathodic polariz

29、ation curves in the absence and in the presence of inhibitor at different concentrations after 30 min of immersion are shown in Figure 1. From this figure, it can be seen that with the increase of LF-Ch extract concentrations, both anodic and cathodic currents were inhibited. This result shows that

30、the addition of LF-Ch extract inhibitor reduces anodic dissolution and also retards the hydrogen evolution reaction. Table 1 gives the values of kinetic corrosion parameters as the corrosion potential Ecorr, corrosion current density Icorr, Tafel slopes (bc and ba) and inhibition efficiency for the

31、corrosion of mild steel with different concentrations of LF-Ch extract. The corrosion current densities were estimated by Tafel extrapolation of the cathodic and anodic curves to the open circuit corrosion potential. From this table, it can be concluded that: ? The Icorr values decrease with increas

32、ing inhibitor concentration. ? The cathodic Tafel slopes were found to vary over a range of 314 - 222 mV dec-1. Therefore, the cathodic slope value was found to change with increasing concentration of LF-Ch extract in aggressive solutions. This result indicates the influence of the inhibitor on the

33、kinetics of the hydrogen evolution reaction 8. ? The anodic Tafel slopes were found to vary over a range of 231 - 126 mV dec-1. Therefore, the anodic slope value was found to change with increasing concentration of LF-Ch extract in aggressive solutions. This result indicates the influence of the inh

34、ibitor on the kinetics of the dissolution of the mild steel. ? The values of inhibition efficiency (P %) increase with inhibitor concentration reaching a maximum value (78.55%) at 100 mg /L. 129 J. Mater. Environ. Sci. 4 (1) (2021) 127-138 Benali et al. ISSN : 2028-2508 CODEN: JMESCN ? The LF-Ch ext

35、ract is a mixed inhibitor. On the other hand, the Corrosion Rate was determined by the conversion of the corrosion current density ( Icorr) by using the expression 18-19: immC.R ()=3.268x10-3 ( corr. MFe) (5) Yearn. Where MFe is the molecular weight of steel, n is the number of electrons transferred

36、 in the corrosion reaction, and is the density of Fe (g . cm?3). Table 2 gives the values of the corrosion rate (C.R), the polarisation resistance (Rp) and inhibition efficiency for the corrosion of mild steel with different concentrations of LF-Ch extract. From this table, it can be concluded that:

37、 ? The C. R values decrease with increasing inhibitor concentration and the Rp values vary in the opposite direction. ? The values of inhibition efficiency (P %) increase with inhibitor concentration reaching a maximum value (78.50%) at 100 mg /L. -1.0 -3.5 -4.0 -4.5 E (mV vs SCE) Figure 1. Potentio

38、dynamic polarization curves for mild steel in 0.5 M H2SO4 +5% EtOH containing different concentrations of LF-Ch extract at 32 C. Table 1. Electrochemical parameters and the corresponding corrosion inhibition efficiencies for the corrosion of mild steel in the presence of different concentrations of

39、LF-Ch extract at 32 C. Conc. Ecorr Icorr ba -bc P% 2 (mg/L) (mV vs CSE) (mA /cm) (mV/dec) (mV/dec) (Icorr) Blank -487 6.9 231 314 - 12.5 -484 4.21 164 265 38.98 25 -478 2.99 138 249 56.67 50 -483 1.85 133 234 73.18 75 -483 1.59 126 228 76.96 100 -486 1.48 127 222 78.55 130 J. Mater. Environ. Sci. 4

40、(1) (2021) 127-138 Benali et al. ISSN : 2028-2508 CODEN: JMESCN Blank 6.85 80.72 - - 36.28 38.95 25 13.85 34.98 50.54 56.66 50 22.50 21.69 66.40 73.13 75 25.30 18.58 72.92 76.98 100 27.65 17.35 75.23 78.50 3. 2. Electrochemical impedance spectroscopy measurements ? Nyquist plots of mild steel in 0.5

41、 M H2SO4 + 5% EtOH in the presence and absence of different concentrations of LF-Ch extract at 32C and after 0.5 h of immersion are given in Figure 2. All the plots display a single capacitive loop 20. Impedance parameters derived from the Nyquist plots and percent inhibition efficiencies are given

42、in Table 3. 15 Table 2. Electrochemical parameters and the corresponding corrosion inhibition efficiencies for the corrosion of mild steel in the presence of different concentrations of LF-Ch extract at 32 C. Conc. Rp C.R P% P% 2 (mg/L) (? ) (mm/Y) (RP) (C.R) 12 - Z (?. cm) 2 9 Im 6 3 2 ZRe (?. cm)

43、Figure 2. Complex plane plots for mild steel in the aggressive solution in the absence and in the presence of different concentrations of LF-Ch extract at 32C. The circuit consists of a constant phase element (CPE) Q, in parallel with a resistor Rt The use of CPE-type impedance has been extensively

44、described 2123: ZCPE=Q(jw)n?1 (6) The above equation provides information about the degree of non-ideality in capacitance behavior. Its value makes it possible to differentiate between the behavior of an ideal capacitor (n = 1) and of a CPE (n < 1). Considering that a CPE may be considered as a p

45、arallel combination of a pure capacitor and a resistor that is inversely proportional to the angular frequency, the value of capacitance, Cdl, can thus be calculated for a parallel circuit composed of a CPE (Q) and a resistor (Rt), according to the following formula 24, 25: (cdlRt)n Q= (7) Rt 131 J. Mater. Environ. Sci. 4 (1) (2021)