The synergistic effect of NaHSO4 and NaCl salts on corrosion inhibition performance of two Gemini ca

来源 :Advanced Materials Science and Technology | 被引量 : 0次 | 上传用户:bye_bye
下载到本地 , 更方便阅读
声明 : 本文档内容版权归属内容提供方 , 如果您对本文有版权争议 , 可与客服联系进行内容授权或下架
论文部分内容阅读
  Abstract In this study, two imidazolium-based ionic liquid surfactants (TSIL and EFAIL) were first synthesized, and then investigated the synergistic effects of NaHSO4 and NaCl salts on corrosion inhibition performance of TSIL and EFAIL inhibitors on low carbon steel samples in 1M HCl solution. For this aim, the electrochemical techniques of potentiodynamic polarization and electrochemical impedance spectroscopy (EIS), surface morphology analyses, and quantum chemical calculations were employed. Results showed that adding salts to acidic solutions containing EFAIL and TSIL increased their inhibition efficiency. Furthermore, addition of NaHSO4 to TSIL-containing solution could further increase the inhibition efficiency compared to other mixtures of the salts and the inhibitors. The DFT results also revealed that the energy gap of TSIL is lower than that of EFAIL, implying that TSIL has more chemical reactivity and less kinetic stability than EFAIL.
  Keywords: Ionic Liquid Surfactant; EIS; Polarization; Acid Corrosion; Surface Tension; Density Functional Theory
  1. Introduction
  Because of having excellent mechanical properties of carbon steel, this metal is widely applied in many industries. The solutions of acidic are also employed in various industries for acid cleaning equipment, steel pickling process, leather processing, and acidization of oil etc. [1,2] The two popular acids consumed for this purpose are hydrochloric and sulfuric acids. These two acids are severely corrosive acid and they can cause severe dissolution of steel. So, slow resistance of steel against acidic environments is a very important problem. In industry, various methods are used to protect steels against corrosion. The most excellent and convenient method of steel protection is use of inhibitor compounds in corrosive media [3–6]. To control, reduce, and prevent interactions between metal surface and corrosive environment, these compounds are added in corrosive environment [7–14]. The most excellent and efficient inhibitors are heterocycle compounds having π bonds and heteroatoms like sulfur, phosphorus, oxygen, and nitrogen in their structures [15–18]. On the other hand, most of inhibitor compounds are toxic and carcinogenic materials affecting the environment. Researchers have tried to find inhibitors with less toxicity and high compatibility with the environment. One of these compounds is ionic liquid (IL) [19,20]. Some IL compounds are known as nontoxic and environmentally friendly compounds for protection of the steel corrosion in acidic media. Ionic liquids have been introduced for the first time in 1914 by reporting the synthesis and physical properties of ethyl ammonium nitrate ionic liquid compound [21–24]. Ionic liquids are melted salts having asymmetric and huge organic cations as well as mineral anions. The melting point of the ionic liquid compounds is below 100 °C and is usually close to room temperature. Ionic liquids are a three-dimensional lattice of cations which are linked together by a subtle energy-balance between dispersion force, hydrogen bonds, and electrostatic interactions. These compounds have many excellent physicochemical properties, such as high electrical conductivity, low vapor pressure and volatility, wide liquidus range, high thermal stability, and no flammability hazard [25]. Because of these features, many compounds of ionic liquids are known as nontoxic and environmentally friendly compounds [22,26,27].   The synergistic effect of ionic liquids in the presence of other compounds has been considered to improve inhibition properties of the inhibitors and reduce costs [28]. There are some reports about studying synergistic effect between halide ions (such as Cl?, Br?, I?), and N-heterocyclic inhibitors for steel corrosion in acidic media. It has been demonstrated that the mixtures of o-phenanthroline/Cl? [29–31], pyrazole/halides [32], triazole derivative/I? [14], and imidazoline derivative/I? [33] have been shown synergistic effects. It has been found that the addition of halide ions to the inhibitor-containing solutions can increase the inhibition effect of inhibitors. The order of inhibition effect of some halides is I?>Br?>Cl?. One reason mentioned for the most synergistic effect of I? is its larger size (216 pm) and higher ability to polarize compared to other halides [34–36].
  The inhibition synergistic effect of adenine and iodide ion (I?) in the H2SO4 solution has been studied [37]. In the study, it was found that the addition of iodide ions to solution containing adenine increase significantly inhibition efficiency value. Moreover, it was indicated that the inhibition mechanism in the presence of iodide ions occurs by electrostatic adsorption of protonated adenine on the surface charged via adsorption of iodide ions on low carbon steel surface.
  In the other research work, the synergistic effect investigation of I? ions and polyacrylamide (PA) on the pure iron corrosion in H2SO4 solution indicated that inhibition performance of the PA is increased in the presence of I? ions, due to simultaneous adsorption of I? ions and PA  molecules on the surface of carbon steel sample [38].
  In the present study, the synergistic effects of two salts containing ions of chloride (Cl?) and sulfate hydrogen (HSO4?) on the inhibition properties of two surfactant inhibitors (TSIL and EFAIL) in HCl solutions has been studied. For this purpose, electrochemical techniques of EIS and potentiodynamic polarization, surface morphology analyses, and as well as quantum chemical calculations were utilized.
  2. Methods
  2.1. Materials and solutions
  Table 1 listed the chemical composition of the low carbon steel samples (20 mm×40 mm×1.5 mm) that were prepared by Esfahan Foolad Mobarakeh Company.
  The TSIL and EFAIL inhibitors were synthesized as new corrosion inhibitors in our laboratory. The chemical structure and full name of these inhibitors is given in Fig. 1. The synthesized inhibitor compounds were completely analyzed by 1H-NMR, 13C-NMR, and FT-IR, which the obtained results brought in S1.   The effects of NaHSO4 and NaCl salts on inhibition properties of TSIL and TFAIL inhibitors were studied in acidic solution (1M HCl). The salts and HCl solution were prepared from Merck Co. To prepare corrosive solution (1M HCl), 37% HCl (Analytical grade) was added to double distilled water.
  Then, 15 mg/L of the inhibitors as well as 0.001 M of NaHSO4 and NaCl salts were added to the prepared corrosive solutions. Before the corrosion test, the low carbon steel samples were mechanically polished with different emery papers grades (400, 600, 800, and 1200). They were washed with acetone and distilled water. Finally, for the cleaning of rust products on metal surface, the samples were immersed in 5% v/v HCl solution for 2-3 s, then rinsed and dried.
  2.2. Characterization of the inhibition performance
  2.2.1. Electrochemical methods
  The effects of NaHSO4 and NaCl salts on inhibition properties of the TSIL and EFAIL inhibitors on the steel surface in acidic solution were investigated by potentiodynamic polarization and electrochemical impedance spectroscopy (EIS) techniques. For this purpose, an Ivium Vertex instrument (Ivium potentiostat/galvanostat) was used. The measurements were performed on a conventional three electrode cell, including working electrode (low carbon steel sample), reference electrode (Ag/AgCl/KCl), and counter electrode (graphite). Both experiments were carried out on 1cm2 of the samples and the rest of the samples were masked with a mixture of beeswax and colophony resin (3:1). The polarization measurements were performed at 1 mV/s scan rate (from -100 mV to +100 mV) at OCP (open circuit potential) condition. EIS was carried at OCP in the frequency scan of 10 kHz to 10 MHz.
  2.2.2. Surface analyses of the steel samples
  Panels of the low carbon steel were immersed to HCl solutions containing NaHSO4 and NaCl salts as well as the EFAIL and TISL inhibitors. The surface morphology of the steel samples was characterized by SEM model AIS2100 after 1 h immersion in the corrosive solutions. The surface tension values were measured by Wilhelmy Technique on a KRUESS PROCESSOR TENSIOMETER K14 V3.07 at 25 ?C temperature.
  By an OCA 15 plus type measuring system was measured the static contact angle of water on the metal surface. For this purpose, a small drop of the solutions was dripped on the surface of the samples. Then, after 10 seconds, the drop shape was recorded by a camera.
  3. Results and discussion   3.1. Determination of critical micelle concentration (CMC)
  The critical micelle concentration (CMC) is a well-known parameter for characterizing behavior of a surfactant in a specific solution. Both the nature of the aqueous environment and the chemical composition of the surfactant affect the CMC point. Therefore, the surface tension values of the solutions containing different concentrations of the EFAIL and TSIL inhibitors were measured (Fig. 2).
  According to Fig. 2, for both the surfactants, the surface tension values decreased by the addition of their concentrations. The decrease in the surface tension can be attributed to the migration of the surfactant molecules from the solution to the surface and replacing water molecules at the surface. The CMC points can be obtained from the break points in the graphs. Therefore, the CMC values of 5 and 15 mg/L were obtained for the solutions containing the EFAIL and TSIL, respectively. These observations indicated that the EFAIL decreased the surface tension and CMC more than the TSIL. The only difference between the molecules of the EFAIL and TSIL is their anions (Cl? in TSIL and HSO4? in EFAIL). Size of HSO4? ion is larger than Cl? ion size. Therefore, HSO4? is less hydrated which plays a very important role in neutralizing surface charges on the micelle surface leading to lower CMC and the surface tension.
  3.2. Electrochemical studies
  3.2.1. Measurements of potentiodynamic polarization
  Polarization plots of low carbon steel immersed in 1M HCl solutions comprising 15 mg/L of the TSIL and EFAIL inhibitors and 0.0001 M of NaCl and NaHSO4 salts are represented in Fig. 3. The electrochemical parameters of corrosion potential (Ecorr), corrosion current density (icorr), and polarization resistance (Rp) obtained from polarization curves are represented in Tables 2 and 3.
  According to Figs. 3(a) and (b), both anodic and cathodic reactions are blocked in the presence of the TSIL and EFAIL inhibitors. The shift of the Ecorr towards less negative values relates to the dominant blocking of anodic reaction compare with the cathodic reaction using the molecules of the two inhibitors.
  It is clear from Tables 2 and 3 that the addition of the TSIL and EFAIL inhibitors to the acidic solution caused a decrease in corrosion current density as well as shift of corrosion potential to more positive values. This probably means that the steel surface behaves like a noble metal surface because of the adsorption of the inhibitor molecules and the formation of the protective layer on the surface of the metal, as well as reduction of the iron anodic dissolution due to the addition of the TSIL and EFAIL concentration, and finally protection of the metal surface from corrosion. Moreover, it can be seen that the EFAIL inhibited corrosion reaction much greater than the TSIL. The EFAIL decreased corrosion current density of the steel immersed in HCl solution much greater than the TSIL. This means that the type of surfactant anion is an effective and important factor on inhibition properties. The inhibitor with HSO4? anion showed higher inhibition efficiency than the one with Cl?. Both the size and charge of the anions are effective parameters on the inhibition properties of the surfactants. The values of inhibition efficiency were calculated by the following equation [39,40]:   Where IE, i, and iinh represent the inhibition efficiency, corrosion current density in the absence and the presence of the inhibitor, respectively. The comparison of inhibition efficiency values for different samples is illustrated in Fig. 4.
  Fig. 4 shows that adding 0.0001 M NaCl and NaHSO4 salts into the HCl solutions containing the inhibitors increased the inhibition efficiency values. The addition of the salts to the HCl solution inhibited both anodic and cathodic reactions. This means that Cl? and HSO4? ions had a synergistic effect on the inhibition properties of the inhibitors. Fig. 4 indicate that addition of NaHSO4 salt in the acidic solution increase the inhibition efficiency more than NaCl salt. Moreover, Fig. 4 data exhibited that the addition of the two salts to the solution containing the TSIL inhibitor has more increase in the inhibition efficiency values compared with the EFAIL inhibitor.
  3.2.2. EIS measurements
  Electrochemical impedance spectroscopy was also utilized to reveal the synergistic effects of addition of NaHSO4 and NaCl salts to the acidic solutions containing TSIL and EFAIL inhibitors at 25?C. The obtained impedance data are shown as Nyquist and Bode plots in Figs 5 and 6.
  The Nyquist plots are not ideal and perfect semicircles due to probably inhomogeneity and roughness of the surface of the samples [41]. Generally, in the evaluation of the Nyquist diagrams, the actual impedance difference at the lower and higher frequencies created the charge transfer [42]. In the present Nyquist diagrams, the semicircles with alone one time constant were obtained, indicating that the charge transfer process dominated the steel corrosion process into the studied corrosive media. Therefore, the expansion of the semicircles indicates a tendency for increasing the charge transfer resistance as the concentration of the inhibitors and salts increases [43]. The addition of the TSIL does not significantly alter the shape of the Nyquist plots, but the form of semicircles be changed in the presence of EFAIL. This may indicate the constitution of a strong adsorption layer upon the surface of the metal. The equivalent circuits presented in Fig. 5 are utilized to extract some electrochemical parameters from impedance data. For more accurate fit of impedance data, CPE (Constant Phase Element) parameter be applied in lieu of double layer capacitance (Cdl). The CPE parameter is obtained from Y0 and n parameters. These parameters are the magnitude and exponent of CPE, respectively. The n parameter shows the roughness or heterogeneity of the electrode surface.   The corrosion inhibition efficiency (IE%) and capacitance (C) were calculated by using the following formulas [44–46]:
  Where Rp and Rp(inh) represent the polarization resistance without and with the inhibitors, respectively. The impedance data and electrochemical parameters for both inhibitors are shown in Tables 4 and 5.
  According to Tables 4 and 5, addition of TSIL and EFAIL inhibitors to the acidic solution lead to an increase in Rp and decrease in C. This means that water molecules are replaced with the molecules of EFAIL and TSIL on the metal surface. The inhibitor layer adsorbed on the metal surface has dielectric constant value lower than water molecules. This finding demonstrates formation of a protective inhibitor layer on the metal surface in HCl solutions containing TSIL and EFAIL. The obtained results show higher inhibition efficiency of EFAIL than TSIL. Tables 4 and 5 show that the addition of 0.0001 M of NaCl and NaHSO4 salts to the acidic solutions containing 15 mg/L of EFAIL and TSIL inhibitors, increases the inhibition efficiency values. In the presence of NaCl and NaHSO4 salts, the Rp value is increased, while C value is decreased. This observation can also show the synergistic effects of salts on increasing the inhibition action of the inhibitors. It is also obvious from the results shown in Tables 4 and 5 that NaHSO4 salt shows higher synergistic effect than NaCl, and NaHSO4 salt shows more increase in the inhibition efficiency value.
  The results of phase angle at 10 kHz and impedance at 10 mHz obtained from Bode plots are presented in Fig. 7.
  According to Fig. 7, impedance at 10 mHz is increased in the presence of the inhibitors. Moreover, the addition of salts caused a further increase in corrosion inhibition efficiency of the inhibitors. The synergistic effects of salts were again found from the results obtained from Bode plots. At 10 kHz, the phase angle is a parameter that indicates capacitor of inhibition layer absorbed on the metal surface [47].
  As can be seen in Fig. 7, the angles of contact were compared between samples immersed in acidic medium containing TSIL and EFAIL and samples immersed in an inhibitor-free solution. It was found that the contact angle at 10 kHz in the acidic medium containing inhibitor was much more negative than the blank medium. The most negative phase angle values were obtained in the presence of both inhibitors and salts. This means that the addition of salts caused more negative phase angle values. The phase angle is negative, and so electrochemical behavior becomes more capacitive. The inhibitor molecules adsorbed on the metal surface show high charge transfer resistance indicating low current tendency to pass through double-layer capacitance. It can again be seen that NaHSO4 had more effect on phase angle than NaCl.   3.3. Surface morphology studies
  3.3.1. SEM
  Fig. 7 represent the SEM micrographs of samples after 1h immersion in the acidic solutions containing the EFAIL and TSIL inhibitors in the presence and absence of salts.
  Fig. 8(a) illustrates that the steel surface exposed to HCl solution without the inhibitor was strongly damaged via chloride anion, and the extreme carbon steel dissolution was observed. It can be seen that wide and deep holes formed on this sample and porosity of the metal surface increased considerably. But by addition of the inhibitors (TSIL and EFAIL) to the acidic solution has been reduced damage of the surface as well as surface porosity, and the surface morphology of the carbon steel sample obtains a significant improvement. Fig. 8 makes it clear that the damage of the surface reduced further by the addition of salts.  For the steel immersed in an acidic solution containing the EFAIL was seen a surface of smoother with porosity and degradation of lower than TSIL. Moreover, addition of the NaHSO4 caused the lowest surface damage and porosity, indicating that the inhibition effect of the inhibitors was enhanced in the presence of this salt more than NaCl. Accordingly, the SEM results are well in accordance with the other obtained results.
  3.3.2. Measurements of the contact angle
  The measurement of the contact angle with water droplet was done on the steel surface exposed to solutions of 1M HCl in the presence and absence of the inhibitors. The result of measurement of the contact angle is illustrated in Fig. 9.
  As depicted in Fig. 9, the water contact angle on the fresh bare steel is about 106?. The contact angle was significantly reduced for the sample exposed to HCl solution without inhibitor. This is probably because of the severe corrosion of the metal in HCl solution, and so corrosion product remaining on the steel surface increases the roughness of the surface. It is clear in Fig. 9 that the addition of inhibitors caused a lower decrease in contact angle. It demonstrates the adsorption of the inhibitor molecules on the metal surface, which protected the surface against corrosion. As a result, surface roughness did not increase significantly due to the lower production of corrosion products on the metal surface. The decreasing contact angle on the sample exposed to the HCl solution containing EFAIL was noticeably lower than the one immersed in the solution with TSIL. This observation demonstrates that EFAIL prevented metal surface from corrosion more efficiently than TSIL. The EFAIL layer adsorbed on the metal surface also makes it more hydrophobic compared to a blank sample.   3.4. Calculation of quantum chemical parameters
  Based on many previous published researches, the molecular electronic structure and molecular geometry structure are related to the inhibition performance of the inhibitor compounds [48–50]. Therefore, the density functional theory (DFT) calculations were used to compare the effects of NaHSO4 and NaCl salts on the inhibition performance of the TSIL and EFAIL. Full geometry optimizations of the TSIL and EFAIL molecules were performed without any symmetry constraints with B3LYP exchange-correlation functional theory [51–53]. Along with this method, the standard basis set of 6-31+G* Pople was used in Gaussian 98 package [54]. Harmonic vibrational frequencies were also evaluated to the determination of the minimum stationary points as a demonstration of the equilibrium structures. As such, the energies of the highest occupied molecular orbital (EHOMO) and the lowest unoccupied molecular orbital (ELUMO), and as well as the energy gap (ΔE=ELUMO-EHOMO) were calculated for obtaining the optimized structures. To gain a better understanding of the inhibition mechanism of the TSIL and EFAIL inhibitors, the required quantum chemical parameters were calculated. Fig. 10 shows the optimized geometric structures and electron density distributions of LUMO and HOMO orbitals of the TSIL and EFAIL inhibitor molecules, as well as imidazolium-based cation (Im) of the two inhibitors. The values of parameters calculated using quantum chemical calculations are reported in Table 6. The molecular orbital theory of Frontier is mostly dependent on tendencies to donate or accept electrons. Therefore, high energy level of HOMO orbitals indicates strong ability of the molecule for donating electrons to good acceptor molecules with empty molecular orbital and low LUMO energy level. The high HOMO energy level of an inhibitor molecule indicates existence of a strong interaction of the molecule and the metal surface. As clearly observed in Table 6, the HOMO molecular orbital energy level of the imidazolium-based cation in the absence of NaHSO4 and NaCl salts is lower than the TSIL and EFAIL inhibitors, indicating that the inhibition efficiency of the Im cation is intensified in the presence of NaHSO4 and NaCl salts. According to the values provided in Table 6, the highest occupied molecular orbital (HOMO) energy level of TSIL is –5.565 eV, which reveals the better inhibition efficiency of the TSIL inhibitor molecules compared to the EFAIL molecules. On the other hand, the HOMO energy level of the EFAIL molecule is obtained –6.535 eV value due to the presence of HSO4– ions in its structure. Furthermore, the energy gap (?EHOMO–LUMO) is a key factor for chemical reactivity of the inhibitor molecules.   Whatever the ?EHOMO–LUMO value of molecules of an inhibitor be smaller, the inhibitory efficiency of the molecules has higher level. The obtained results show that the energy gap of the TSIL molecule is lower than that of EFAIL molecule, implying that the TSIL has more chemical reactivity and less kinetic stability than EFAIL.
  3.5. Inhibition mechanism of surfactants in the presence and absence of salts
  When the steel is placed in a hydrochloric acid solution, its surface becomes positively charged. Therefore, Cl? or HSO4? ions tend to be adsorbed on the positively charged sites changing the surface charge into negative charge. In the next step, the EFAIL and TSIL molecules can interact with metal surface, and so forms monomolecular layers on the surface.
  The inhibitor molecules could also reduce the hydrogen evolution reaction of H+ ions at cathodic regions on the metal surface. Adding salt causes several effects, one of which may be decrease in CMC and surface tension. This effect could be attributed to compressing the electrical double layer surrounding micelles, which decreases the electrostatic repulsion between the polar heads of compounds. Therefore, the CMC occurs at a lower concentration in comparison with solutions without salts. In other words, the effect of salts in the solution can be attributed to a change in the ionic force of the solution and also an effect on the ionic force of the EFAIL and TSIL. Since the anion of salt decreases the solubility of the inhibitor molecules, the EFAIL or TSIL molecules prefer to form micelles at lower concentrations. It has been shown that adding NaHSO4 to the inhibitor-containing solution causes a more effect on its inhibition performance enhancement. HSO4? ion is larger than Cl? one. Therefore, the HSO4? salt has less hydration that it can be highly effective at neutralizing surface charges of micelle [47].
  4. Conclusions
  The aim of this study is to elucidate the corrosion behaviour of low carbon steel samples in the 1M HCl solution containing mixtures of TSIL and EFAIL inhibitors and NaHSO4 and NaCl salts, as well as investigation of inhibition mechanism of these compounds using the experimental and theoretical approaches. The main results are summarized below.
  The electrochemical results showed that the addition of TSIL and EFAIL inhibitors to the HCl solution caused decrease in the corrosion current density and displacement of corrosion potential towards less negative values. It was shown that the EFAIL inhibitor with HSO4? ions could inhibit corrosion rate significantly as compared to the TSIL inhibitor with Cl? ions.   Addition of salts to 1M HCl solutions containing TSIL and EFAIL inhibitors could inhibit further corrosion of the steel sample surface. In addition, NaHSO4 salt showed better synergistic effect than NaCl salt in the presence of the two TSIL and EFAIL inhibitors, separately.
  The metal surface degradation was obviously decreased in the presence of the inhibitors, especially when the mixture of each inhibitors and salts was used.
  The neutralization of micelle surface charges via HSO4? ions with them larger size and less hydration is more than relatively small Cl? ions with more hydration.
  Reference:
  [1] E. Kamali Ardakani, E. Kowsari, A. Ehsani, Imidazolium-derived polymeric ionic liquid as a green inhibitor for corrosion inhibition of mild steel in 1.0 M HCl: Experimental and computational study, Colloids Surfaces A Physicochem. Eng. Asp. 586 (2020) 124195.
  [2] D. Daoud, T. Douadi, H. Hamani, S. Chafaa, M. Al-Noaimi, Corrosion inhibition of mild steel by two new S-heterocyclic compounds in 1 M HCl: Experimental and computational study, Corros. Sci. 94 (2015) 21–37.
  [3] D. Asefi, M. Arami, N.M. Mahmoodi, Electrochemical effect of cationic gemini surfactant and halide salts on corrosion inhibition of low carbon steel in acid medium, Corros. Sci. 52 (2010) 794–800.
  [4] J. Aljourani, M.A. Golozar, K. Raeissi, The inhibition of carbon steel corrosion in hydrochloric and sulfuric acid media using some benzimidazole derivatives, Mater. Chem. Phys. 121 (2010) 320–325.
  [5] S.K. Shukla, L.C. Murulana, E.E. Ebenso, Inhibitive effect of imidazolium based aprotic ionic liquids on mild steel corrosion in hydrochloric acid medium, Int. J. Electrochem. Sci. 6 (2011) 4286–4295.
  [6] L. Li, Q. Qu, W. Bai, F. Yang, Y. Chen, S. Zhang, Z. Ding, Sodium diethyldithiocarbamate as a corrosion inhibitor of cold rolled steel in 0.5M hydrochloric acid solution, Corros. Sci. 59 (2012) 249–257.
  [7] L.F. Li, P. Caenen, J.P. Celis, Effect of hydrochloric acid on pickling of hot-rolled 304 stainless steel in iron chloride-based electrolytes, Corros. Sci. 50 (2008) 804–810.
  [8] E.M. Sherif, S.M. Park, Inhibition of copper corrosion in acidic pickling solutions by N-phenyl-1,4-phenylenediamine, Electrochim. Acta. 51 (2006) 4665–4673.
  [9] M. Karaku?, M. ?ahin, S. Bilgi?, An investigation on the inhibition effects of some new dithiophosphonic acid monoesthers on the corrosion of the steel in 1 M HCl medium, Mater. Chem. Phys. 92 (2005) 565–571.   [10] E.A. Flores, O. Olivares, N. V. Likhanova, M.A. Domínguez-Aguilar, N. Nava, D. Guzman-Lucero, M. Corrales, Sodium phthalamates as corrosion inhibitors for carbon steel in aqueous hydrochloric acid solution, Corros. Sci. 53 (2011) 3899–3913.
  [11] X. Wang, H. Yang, F. Wang, An investigation of benzimidazole derivative as corrosion inhibitor for mild steel in different concentration HCl solutions, Corros. Sci. 53 (2011) 113–121.
  [12] N.A. Negm, A.M.A. Sabagh, M.A. Migahed, H.M.A. Bary, H.M.E. Din, Effectiveness of some diquaternary ammonium surfactants as corrosion inhibitors for carbon steel in 0.5 M HCl solution, Corros. Sci. 52 (2010) 2122–2132.
  [13] A.S. Fouda, A.S. Ellithy, Inhibition effect of 4-phenylthiazole derivatives on corrosion of 304L stainless steel in HCl solution, Corros. Sci. 51 (2009) 868–875.
  [14] F. Bentiss, C. Jama, B. Mernari, H. El Attari, L. El Kadi, M. Lebrini, M. Traisnel, M. Lagrenée, Corrosion control of mild steel using 3,5-bis(4-methoxyphenyl)-4-amino-1,2,4-triazole in normal hydrochloric acid medium, Corros. Sci. 51 (2009) 1628–1635.
  [15] E.A. Noor, The impact of some factors on the inhibitory action of Radish seeds aqueous extract for mild steel corrosion in 1M H2SO4 solution, Mater. Chem. Phys. 131 (2011) 160–169.
  [16] X.G. Li, M.R. Huang, J.F. Zeng, M.F. Zhu, The preparation of polyaniline waterborne latex nanoparticles and their films with anti-corrosivity and semi-conductivity, Colloids Surfaces A Physicochem. Eng. Asp. 248 (2004) 111–120.
  [17] K. Soeda, T. Ichimura, Present state of corrosion inhibitors in Japan, Cem. Concr. Compos. 25 (2003) 117–122.
  [18] E.B. Ituen, M.M. Solomon, S.A. Umoren, O. Akaranta, Corrosion inhibition by amitriptyline and amitriptyline based formulations for steels in simulated pickling and acidizing media, J. Pet. Sci. Eng. 174 (2019) 984–996.
  [19] S. Kholghi Eshkalak, M. Khatibzadeh, E. Kowsari, A. Chinnappan, S. Ramakrishna, Application of ionic liquids as charge control agents of pigments and preparation of microcapsules as electronic inks through electrospraying, Opt. Mater. (Amst). 84 (2018) 73–81.
  [20] S. Kholghi Eshkalak, M. Khatibzadeh, E. Kowsari, A. Chinnappan, S. Ramakrishna, A novel surface modification of copper (II) phthalocyanine with ionic liquids as electronic ink, Dye. Pigment. 154 (2018) 296–302.
  [21] M.H. Wang, Y.J. Li, Z.X. Xie, C. Liu, E.S. Yeung, Fabrication of large-scale one-dimensional Au nanochain and nanowire networks by interfacial self-assembly, Mater. Chem. Phys. 119 (2010) 153–157.   [22] B. Dong, X. Zhao, L. Zheng, J. Zhang, N. Li, T. Inoue, Aggregation behavior of long-chain imidazolium ionic liquids in aqueous solution: Micellization and characterization of micelle microenvironment, Colloids Surfaces A Physicochem. Eng. Asp. 317 (2008) 666–672.
  [23] M. Corrales-Luna, T. Le Manh, M. Romero-Romo, M. Palomar-Pardavé, E.M. Arce-Estrada, 1-Ethyl 3-methylimidazolium thiocyanate ionic liquid as corrosion inhibitor of API 5L X52 steel in H 2 SO 4 and HCl media, Corros. Sci. 153 (2019) 85–99.
  [24] S. Cao, D. Liu, H. Ding, J. Wang, H. Lu, J. Gui, Task-specific ionic liquids as corrosion inhibitors on carbon steel in 0.5 M HCl solution: An experimental and theoretical study, Corros. Sci. 153 (2019) 301–313.
  [25] E. Kamali Ardakani, E. Kowsari, A. Ehsani, Imidazolium-derived polymeric ionic liquid as a green inhibitor for corrosion inhibition of mild steel in 1.0 M HCl: Experimental and computational study, Colloids Surfaces A Physicochem. Eng. Asp. (2019) 124195.
  [26] N. V. Likhanova, M.A. Domínguez-Aguilar, O. Olivares-Xometl, N. Nava-Entzana, E. Arce, H. Dorantes, The effect of ionic liquids with imidazolium and pyridinium cations on the corrosion inhibition of mild steel in acidic environment, Corros. Sci. 52 (2010) 2088–2097.
  [27] E. Kowsari, M. Payami, R. Amini, B. Ramezanzadeh, M. Javanbakht, Task-specific ionic liquid as a new green inhibitor of mild steel corrosion, Appl. Surf. Sci. 289 (2014) 478–486.
  [28] L. Feng, S. Zhang, Y. Lu, B. Tan, S. Chen, L. Guo, Synergistic corrosion inhibition effect of thiazolyl-based ionic liquids between anions and cations for copper in HCl solution, Appl. Surf. Sci. 483 (2019) 901–911.
  [29] X. Li, S. Deng, H. Fu, G. Mu, Inhibition effect of 6-benzylaminopurine on the corrosion of cold rolled steel in H2SO4 solution, Corros. Sci. 51 (2009) 620–634.
  [30] G.N. Mu, X. Li, F. Li, Synergistic inhibition between o-phenanthroline and chloride ion on cold rolled steel corrosion in phosphoric acid, Mater. Chem. Phys. 86 (2004) 59–68.
  [31] X. Li, L. Tang, L. Li, G. Mu, G. Liu, Synergistic inhibition between o-phenanthroline and chloride ion for steel corrosion in sulphuric acid, Corros. Sci. 48 (2006) 308–321.
  [32] G.K. Gomma, Corrosion of low-carbon steel in sulphuric acid solution in presence of pyrazole-halides mixture, Mater. Chem. Phys. 55 (1998) 241–246.
  [33] P.C. Okafor, Y. Zheng, Synergistic inhibition behaviour of methylbenzyl quaternary imidazoline derivative and iodide ions on mild steel in H2SO4 solutions, Corros. Sci. 51 (2009) 850–859.   [34] A.M. Ridhwan, A.A. Rahim, A.M. Shah, Synergistic effect of halide ions on the corrosion inhibition of mild steel in hydrochloric acid using mangrove tannin, Int. J. Electrochem. Sci. 7 (2012) 8091–8104.
  [35] M.R. Adam, A.A. Rahim, A.M. Shah, Synergy between iodide ions and mangrove tannins as inhibitors of mild steel corrosion, Ann. For. Sci. 72 (2015) 9–15.
  [36] M. Abdallah, S.T. Atwa, M.M. Salem, A.S. Fouda, Synergistic effect of some halide ions on the inhibition of zinc corrosion in hydrocchloric acid by tetrahydro carbazole derivatives compounds, Int. J. Electrochem. Sci. 8 (2013) 10001–10021.
  [37] A.A. Farag, M.A. Hegazy, Synergistic inhibition effect of potassium iodide and novel Schiff bases on X65 steel corrosion in 0.5M H2SO4, Corros. Sci. 74 (2013) 168–177.
  [38] M.M. Solomon, S.A. Umoren, M.A. Quraishi, M.A. Jafar Mazumder, Corrosion inhibition of N80 steel in simulated acidizing environment by N-(2-(2-pentadecyl-4,5-dihydro-1H-imidazol-1-YL) ethyl) palmitamide, J. Mol. Liq. 273 (2019) 476–487.
  [39] G. Cui, J. Guo, Y. Zhang, Q. Zhao, S. Fu, T. Han, S. Zhang, Chitosan oligosaccharide derivatives as green corrosion inhibitors for P110 steel in a carbon-dioxide-saturated chloride solution, Carbohydr. Polym. 203 (2019) 386–395.
  [40] H. Tian, W. Li, A. Liu, X. Gao, P. Han, R. Ding, C. Yang, D. Wang, Controlled delivery of multi-substituted triazole by metal-organic framework for efficient inhibition of mild steel corrosion in neutral chloride solution, Corros. Sci. 131 (2018) 1–16.
  [41] J. Aljourani, K. Raeissi, M.A. Golozar, Benzimidazole and its derivatives as corrosion inhibitors for mild steel in 1M HCl solution, Corros. Sci. 51 (2009) 1836–1843.
  [42] N. V Likhanova, P. Arellanes-Lozada, O. Olivares-Xometl, I. V Lijanova, J. Arriola-Morales, J. Carlos Mendoza-Hernandez, G. Corro, Ionic liquids with carboxylic-acid-derived anions evaluated as corrosion inhibitors under dynamic conditions, Int. J. Electrochem. Sci. 14 (2019) 2655–2671.
  [43] A. D?ner, R. Solmaz, M. ?zcan, G. Kardas, G. Karda?, Experimental and theoretical studies of thiazoles as corrosion inhibitors for mild steel in sulphuric acid solution, Corros. Sci. 53 (2011) 2902–2913.
  [44] B.P. Markhali, R. Naderi, M. Mahdavian, M. Sayebani, S.Y. Arman, Electrochemical impedance spectroscopy and electrochemical noise measurements as tools to evaluate corrosion inhibition of azole compounds on stainless steel in acidic media, Corros. Sci. 75 (2013) 269–279.   [45] W. Li, A. Liu, H. Tian, D. Wang, Controlled Release of Nitrate and Molybdate Intercalated in Zn-Al-Layered Double Hydroxide Nanocontainers towards Marine Anticorrosion Applications, Colloid Interface Sci. Commun. 24 (2018) 18–23.
  [46] J. Du, Y. Liu, P. Liu, Y. Liu, S. Gao, L. Zhang, Effect of Inhibitor based on Emulsion on Mild Steel Corrosion in Acid Environment, Int. J. Electrochem. Sci. 14 (2019) 4532–4545.
  [47] R. Fuchs-Godec, M.G. Pavlovi?, Synergistic effect between non-ionic surfactant and halide ions in the forms of inorganic or organic salts for the corrosion inhibition of stainless-steel X4Cr13 in sulphuric acid, Corros. Sci. 58 (2012) 192–201.
  [48] A.R. Jannat, R. Naderi, E. Kowsari, H. Zandi, M. Saybani, R. Safari, A. Ehsani, Electrochemical techniques and quantum chemical analysis as tools to study effect of a dicationic ionic liquid on steel behavior in H2SO4, J. Taiwan Inst. Chem. Eng. 99 (2019) 18–28.
  [49] A. Ehsani, M.G. Mahjani, M. Hosseini, R. Safari, R. Moshrefi, H. Mohammad Shiri, Evaluation of Thymus vulgaris plant extract as an eco-friendly corrosion inhibitor for stainless steel 304 in acidic solution by means of electrochemical impedance spectroscopy, electrochemical noise analysis and density functional theory, J. Colloid Interface Sci. 490 (2017) 444–451.
  [50] A. Ehsani, M.G. Mahjani, R. Moshrefi, H. Mostaanzadeh, J.S. Shayeh, Electrochemical and DFT study on the inhibition of 316L stainless steel corrosion in acidic medium by 1-(4-nitrophenyl)-5-amino-1H-tetrazole, RSC Adv. 4 (2014) 20031–20037.
  [51] Z. El Adnani, M. Mcharfi, M. Sfaira, M. Benzakour, A.T. Benjelloun, M. Ebn Touhami, DFT theoretical study of 7-R-3methylquinoxalin-2(1H)-thiones (RH; CH3; Cl) as corrosion inhibitors in hydrochloric acid, Corros. Sci. 68 (2013) 223–230.
  [52] L. Guo, S. Zhu, S. Zhang, Q. He, W. Li, Theoretical studies of three triazole derivatives as corrosion inhibitors for mild steel in acidic medium, Corros. Sci. 87 (2014) 366–375.
  [53] I.B. Obot, D.D. Macdonald, Z.M. Gasem, Density functional theory (DFT) as a powerful tool for designing new organic corrosion inhibitors: Part 1: An overview, Corros. Sci. 99 (2015) 1–30.
  [54] E. Kowsari, S.Y. Arman, M.H. Shahini, H. Zandi, A. Ehsani, R. Naderi, A. PourghasemiHanza, M. Mehdipour, In situ synthesis, electrochemical and quantum chemical analysis of an amino acid-derived ionic liquid inhibitor for corrosion protection of mild steel in 1M HCl solution, Corros. Sci. 112 (2016) 73–85.
其他文献
“输入、输出、活动、关系、客户、价值”这六要素的组合给出了流程的定义,即流程是一组存在相互“关系”的“活动”,它最终会将“输入”转化成为对“客户”有“价值”的“输出”。所有了解过流程的人都会首先接触到这个概念,并且在流程管理的过程中不断的应用这个概念,它们来源于传说中的流程管理之父——迈克尔·哈默的流程解释。  流程六要素想必大家已经耳熟能详了。但如果仅仅停留在定义流程的六要素上,在应用流程管理的
期刊
老板为何总是抽身乏术  很多企业老板总是向我们抱怨说:“员工表现不够积极,很多员工决定是否留在企业主要考虑薪资和工作的稳定性,相当一部分人得过且过,甚至可以说在混日子,在现场工作的低层员工更是如此。”“员工的依赖心理十分严重,老板做得越多,员工对他的依赖就越多;老板越能干,下属就越不能干;老板越操心,下面的人就越不操心。”  因此,在企业里,老板与员工的状态往往截然相反:老板忙东忙西、累死累活,员
期刊
只要细心去找,借口无处不在,做不好一件事情,完不成一项任务,有成千上万条借口在那儿响应你、声援你、支持你,抱怨、推诿、迁怒、愤世嫉俗成了最好的解脱。  我们无法改变或支配他人,但一定能改变自己对借口的态度,远离借口的羁绊,控制借口对自己的影响力,坚定完成任务的信心和决心。  美国西点军校在世界之所以久负盛名,不仅因为它培养了一批批优秀的军事人才,更重要的是它还培养出无数商界精英,他们秉承军校的理念
期刊
能力素质模型是岗位任职资格的重要内容,目前正逐渐应用于人才选拔、员工培训等人力资源管理领域。在实际操作中,许多企业更侧重于利用能力素质模型进行人才测评而不是员工能力提升。相比之下,微软公司基于能力素质模型进行的企业知识管理推行值得我们许多企业学习借鉴。  从1995年开始,微软公司就在内部信息技术部门开展了“技能规划与开发”项目,并逐步在全公司推广。该计划分为五个主要阶段:  1.构建知识能力的类
期刊
战略如何落地,我们将其分为三步曲:共识—共鸣—共振。即在战略制定的过程中,使各管理层充分参与研讨,取得对未来发展目标和方向的共识;在战略分解的过程中,各部门的行动计划能横向协同、纵向一致,取得共鸣;在战略执行中能够有计划有节奏地按照既定行动大纲实施落地,产生共振。战略从共识—共鸣—共振的闭环,中间需要有关键管控点,而这些关键管控点即战略管理相关的会议。  关键词:战略落地 战略研讨会 战略规划质询
期刊
基于流程的战略变革的核心是提升企业系统规划与变革能力,提升企业跨部门协同变革能力,提升企业流程变革实施能力,提升企业战略执行精细化能力。基于流程的战略规划有助于企业提升战略执行力,帮助企业完成从战略到执行的转变。  关键词:战略规划 战略落地 战略执行力 流程管理  流程管理之父哈默认为:“在以流程为中心的公司中,对于战略的考虑,并不是考虑企业的产品和服务是否能够获得市场的成功,而是考虑企业的流程
期刊
在平衡计分卡和战略地图构建的构成中引入流程管理的理念和工具,我们期望能够促进分解的科学性和合理性,用流程输出和过程的观念进行引导,用流程架构对分解进行控制,能够避免该项工作开展的无序化,尽可能避免人为因素在当中起到的作用。同时,增强指标、行动与企业实际业务结合的紧密性。  关键词:战略落地 平衡计分卡 流程管理 战略地图  “不能描述就不能衡量,不能衡量就不能管理”。  这是当我们提及平衡计分卡时
期刊
一项调查表明,好战略得到成功实施的比例不足10%。某项权威研究结果显示,从1988年至2000年,在全球1854家大公司中,每8家公司里就有7家未能实现盈利性增长。然而,其中竟然有90%的公司都曾经制定过详尽的战略计划,而且定下了雄心勃勃的战略目标。想必与这些曾经十分热衷战略管理的企业一样,企业家们心里都会有这样的疑问:“战略有用吗?这些战略实施的问题又在哪?”  常常听企业家们说:什么都可以出错
期刊
你说:流程和岗位标准化是什么关系?一个岗位碰到突发情况时怎么办?  我说:中观制度和微观制度相辅相成,在变化中寻找规律。  如果一个人在执行一个流程的某一活动的时候,由于有很多具体情况要判断,构成流程的出现很多分叉走法,以致流程图都写不下了,这该怎么办?实际工作中还会碰到很多突发情况,是流程图里没有画出来、流程里找不到工作指导的,此时该怎么处理?  这是个两难的问题。  如果把所有判断、分叉、YE
期刊
20世纪50年代后期诞生于日本丰田汽车公司的TPS ,在80年代得以发展完善,并逐渐提炼形成一套管理系统——精益生产方式。到了80年代后期,TPS得以在全世界许多企业里得以实施和推广,取得了较为丰硕的成果:生产周期缩短,再制品减少,生产效率提高,废品减少,库存大幅度降低……  在TPS创立之初,丰田公司就开始了致力全员参与消除大规模生产的浪费来降低成本的改善活动,这些活动最终使丰田成为制造行业的领
期刊