ZG/ZH Mannich bases (acid corrosion inhibitors) were synthesized with benzaldehyde, 2-aminothiazole, acetophenone/cyclohexanone as raw materials, and selecting the appropriate proportion of reaction time, temperature and ratio of raw materials.The corrosion inhibition performance of two kinds of Mannich bases on N80 steel was investigated by means of mass loss method and electrochemical technique. The result of mass loss method showed that two kinds of inhibitors both had excellent effect on N80 steel in 15% hydro-chloric acid solution. Electrochemical technique showed that both ZG and ZH were a mainly anodic-controlling composite corrosion inhibitor, and their corrosion inhibition effect was further confirmed by AC impedance technique. The adsorption behavior between inhibitiors and the steel surface both abides by the Langmuir isotherm model.
Mild steel is one of the most extensively used constructional materials in industries due to its low cost and prominent mechanical properties. However, mild steel is easily eroded in the process of dealing with it such as acid cleaning, pickling and so on [1] [2] . In order to solve this problem, it is strongly necessary to add an inhibitor to protect mild steel from corrosion [3] [4] . Adding anti-corrosion inhibitor is relatively simple, efficient and economic approach to protect metals in acid media [5] [6] [7] [8] [9] .
The Mannich bases are famous acid inhibitors containing N, O and S atoms, and these atoms of high electron density generate multiple bonds through which they are adsorbed on metal surface, preventing corrosion reaction of N80 steel from acid media. The polar functional groups are commonly viewed as the reaction center for the establishment of the adsorption process [10] [11] [12] [13] . The Mannich base acts as a corrosion inhibitor due to the presence of the hetero atoms. The Mannich reaction is a three component condensation reaction in which an active H atom is allowed to react with an aldehyde or ketone and amine, concomitant release of water to produce a new base known as a Mannich base. On the basis of two new-type of synthesized acid corrosion inhibitors via mannich reaction, its reaction condition-reaction temperature may be less than 100˚C, and reaction pressure in room may not need to change, and reaction time may be transient-can get moderate. In general, containing more than three phenyl rings, the large molecule of synthesized compound has poor performance of water solubility. With the increase of phenyl ring, the water solubility of compound decreases obviously. Molecules of corrosion inhibitors in this paper include not more than two phenyl rings, and both of corrosion inhibitors can dissolve easily in water. Raw materials of synthesized ZG/ZH Mannich bases perform excellent inhibition efficiency respectively, due to containing O or Cyclobenzene. 2-aminothiazole is a kind of excellent traditional corrosion inhibitor, and contains N and S atoms. 2-aminothiazole was modified as acid corrosion inhibitors by mannich reaction. ZG/ZH Mannich bases were synthesized with benzaldehyde, 2-aminothiazole, acetophenone/cyclohexanone as raw materials. The corrosion inhibition performance of two kinds of Mannich bases on N80 steel was studied by means of mass loss method and electrochemical technique. In view of structures and performances of corrosion inhibitors, author can get more research about corrosion.
2. Experimental
Materials. N80 steel sheets were pretreated by grinding with abrasive paper then cleaned with double-distilled water, degreased with acetone and dried at room temperature before doing the experiment. The way of preparing 15% hydrochloric acid is diluting of analytical grade 37% HCl with distilled water.
Inhibitors. ZG/ZH Mannich bases (acid corrosion inhibitors) were synthesized with benzaldehyde, acetone, aniline/benzylamine as raw materials. Appropriate proportion of reaction time, temperature and ratio of raw materials were se- lected. The molecular structure of studied compounds were given as Scheme 1, Scheme 2.
Scheme 1. Structure and synthetic route of ZG.
Scheme 2. Structure and synthetic route of ZH.
2.1. Weight Loss Method
Weight loss experiments were carried out in accordance with the standard of SY5405-1996. All the tests were done in aerated 15% HCl.
The corrosion rate (ν) in g・m−2・h−1 was determined from the following re- lationship:
where W and W0 are the weight loss in the presence and absence of inhibitors, t is the corrosion time (h), and S is the area of specimen (m2).
The inhibition efficiency (η) was determined from the following relationship:
where, v and v0 are the corrosion rates of the N80 steel in the presence and absence of inhibitors
2.2. Electrochemical Studies
Electrochemical Impedance (EI) and Tafel polarization were conducted in aerated 15% HCl in CHI660E electrochemical work station at room temperature. A conventional three-electrode system [14] consisting of platinum as counter electrode, a saturated calomel electrode as reference electrode, and N80 steel as working electrode were used. The EI measurements were acquired at a corrosion potential over a frequencyrange of 0.1~100 kHz with signal amplitude of 5 mV. The Tafel polarization measurements were conducted for a potential range of −300 mV to −600 mV with respect to open circuit potential, at a scan rate of 1 mV・s−1.
3. Results and Discussion3.1. Mass Loss Studies
The corrosion rates of different concentrations of inhibitor ZG/ZH in 15% hydrochloric acid for an exposure time 4 h at 60˚C are presented in Figure 1.
The corrosion rate of different concentrations of ZH/ZG in 15% hydro- chloric acid
The results indicated that the corrosion rates of N80 steel in 15% hydrochloric acid were 0.4362 g・m−2・h−1 of inhibitor ZG and 0.7118 g・m−2・h−1 of inhibitor ZH when the dosage of inhibitor added respectively was 1.0%, which is much higher than national standard. With increase of concentrations of inhibitor ZG/ZH, the corrosion rate of N80 steel in 15% hydrochloric acid decreases respectively, and they prevent effectively the metal surface from water and corrosive medium in the liquid [15] .
3.2. Electrochemical Studies
Polarization studies. Tafel polarization for N80 steel in 15% hydrochloric acid in the obsence and presence of different concentration of inhibitor ZG, inhibitor ZH at room temperature are shown in Figure 2.
Figure 2 represents the polarization curves of N80 steel in 15% HCl in the absence and presence of various concentrations of ZG and ZH. It can be seen from Figure 2 that, in the presence of inhibitors, the curves are shifted to lower current regions, showing the inhibition tendency of the Mannich bases. There was definite trend observed in the Ecorr values in the presence of both the Mannich bases. In the present study, shift in Ecorr values is in the range of 0.010~0.030 V suggesting that they all act as mixed type inhibitors.
The values of various electrochemical parameters derived by Tafel polari- zation of the inhibitors are given in Table 1. Investigation Table 1 revealed that the values of ba increase orderly in the presence of both the inhibitors, indicating that both anodic and cathodic reactions are affected but the effect on the anodic reactions is more prominent. Thus, both ZG and ZH acted as mainly anodic- controlling composite corrosion inhibitors [16] . In the same circumstances, according to Icorr, ZG has higher inhibition efficiency than that of ZH.
Polarization curves of N80 steel with different concentrations of ZH/ZG inhibitor
The electrochemical parameters for N80 with different concentrations ZG/ZH inhibitor
inhibitor
Conc.
Ecorr/v
Icorr/(A・cm−2)
Ba/(mv・dec−1)
Bc/(mV・dec−1)
blank
15% HCl
−0.456
1.074 × 10−3
6.566
4.083
ZG
0.3%
−0.452
1.000 × 10−4
6.914
6.743
0.5%
−0.449
9.218. × 10−5
7.034
5.030.
0.7%
−0.447
9.088 × 10−5
7.195
5.666
1.0%
−0.440
8.419 × 10−5
8.890
6.218
ZH
0.3%
−0.451
1.147 × 10−4
6.740
6.338
0.5%
−0.442
1.069 × 10−4
7.034
7.743
0.7%
−0.432
9.938 × 10−5
6.906
6.794
1.0%
−0.425
9.933. × 10−5
8.345
5.653
3.3. AC Impedance Studies
Nyquist plots of N80 steel plate in 15% hydrochloric acid in the obsence and presence of different concentration of inhibitor ZG，inhibitor ZH at room temperature are presented in Figure 3.
The Nyquist figure of N80 steel with different concentrations of ZG/ZH inhibitor
Impedance parameters can be calculated from Nyquist plot via equivalent circuit to fit the impedance data, which are presented in Figure 4.
Equivalent circuit to fit the impedance data
The corrosion of N80 steel in 15% HCl solution in the absence and presence of ZG and ZH were investigated by EI. Nyquist plots for N80 steel obtained at the interface in the absence and presence of inhibitors at different concentrations are given in Figure 3.
The Nyquist diagram obtained with 15% HCl shows only one capacitive loop and the diameter of the semicircle increases on increasing the inhibitor concentration suggesting that the formed inhibitive film was strengthened by the addition of inhibitors. All the main parameters deduced from the impedance technique are given in Table 2.
The AC impedance coefficient during the corrosion process
inhibitor
Conc.
Rs/(Ω・cm−2)
CPE-T/(F・cm−2)
CPE-P/1
Rp/(Ω・cm−2)
blank
15% HCl
0.658.
1.92 × 10−4
0.64114
46.2
ZG
0.3%
1.024
1.25 × 10−4
0.66755
332.7
0.5%
1.463
1.09 × 10−4
0.69163
557.9
0.7%
2.513
1.12 × 10−4
0.69627
733.5
1.0%
2.928
1.05 × 10−4
0.69231
809.9.
ZH
0.3%
0.799
1.42 × 10−4
0.66957
213.3
0.5%
2.157
1.17 × 10−4
0.67694
395.4
0.7%
2.626
1.13 × 10−4
0.67581
431.7
1.0%
2.513
1.08 × 10−4
0.69627
733.5
3.4. Analysis of Adsorption Mechanism
Adsorption isotherm. Surface coverage (θ) was regarded as η nearly and was tested by mass loss method in 15% hydrochloric acid in accordance with the standard of SY5405-1996.
The values of the concentration of inhibitor (c) and θ were evaluated by conforming to various isotherms like Bockris-Swinkels [17] , Langmuir [18] and Frumkin [19] . However, in this experiment the best fit was subject to Langmuir adsorption isotherm as presented in Figure 5.
Langmuir adsorption isotherm (3)
The relationship can be changed to: (4)
where, K is the equilibrium constant for the process of desorption/adsorption.
Adsorption isotherm of ZH/ZG inhibitor
According to Figure 5, The plot of c against c/η was nearly a straight line. It expressed that inhibitor formed a monolayer adsorption on N80 steel. K can be calculated which is related to free energy of adsorption, ΔGm, as given by following equation:
where Csolvent is concentration of water in solution, is 55.5 mol/L, R = 8.314 (J・mol−1・K−1).
Thermodynamic parameters for the adsorption of inhibitors in 15% HCl on the N80 steel at 60˚C was given in Table 3.
The thermodynamic parameters of the adsorption process
inhibitor
R2/1
Kads/(L・mol−1)
/(kJ・mol−1)
ZG
0.09993
1.3746
−13.25
ZH
0.09998
0.9018
−12.50
The negative value of ΔG m suggests that inhibitor molecules are spontaneously adsorbed on steel surface. More negative ΔGm means more the strength of adsorption. It accepted that the values of ΔGm up to −20 kJ・mol−1, the types of adsorption were regarded as physisorption, while the values around −40 kJ・mol−1 or smaller, were seen as chemisorptions. In this study the value of ΔGm was up to −20 kJ・mol−1, which means the possibility of both physisorption.
Effect of temperature. The effect of temperature on the performance of the inhibitors for N80 steel plate in 15% hydrochloric acid at 20˚C, 40˚C, 60˚C, 80˚C was researched using weight loss methods, when the dosage of inhibitor added was 1.0%. The apparent activation energy (Ea) for the corrosion reaction of N80 steel in 15% hydrochloric acid can be calculated from Arrhenius equation [20] :
The relationship can be changed to: (7)
where A is the Arrhenius pre-exponential constant. Plots of lnVcorr against 1/T are shown in Figure 6.
The Arrhenius curve of ZH/ZG inhibitor
According to Figure 6, the value of Ea of the corrosion reaction of N80 steel in 15% hydrochloric acid in the obsence of inhibitor was 23.986 KJ/mol. Adding the inhibitors ZG/ZH makes the values of Ea of the corrosion reaction more than 30 KJ/mol. and makes corrosion rate of N80 steel decreased sharply.
4. Conclusions
1) ZG/ZH Mannich bases were synthesized with benzaldehyde, 2-amino- thiazole, acetophenone/cyclohexanone as raw materials, and the corrosion rate of N80 steel in 15% hydrochloric acid was much higher than national standard respectively when the dosage of inhibitor added was 1.0%.
2) The negative value of ΔGm obtained from this study indicated that these compounds are absorbed spontaneously on the N80 steel surface.
3) The absorption of ZG/ZH inhibitor was subjected to Langmuir absorption isotherm.
4) Electrochemical technique showed that both ZG and ZH act as a mainly anodic-controlling composite corrosion inhibitors, and ZG has higher inhibition efficiency than that of ZH, which accorded well with results of Weight loss studies.
Acknowledgements
Thanking Zhou Shu-sheng, Tang Tian-tian and Shi Dong-po for their assistance. and the research was supported by two Fund project: National natural science foundation (41202111) and Hubei provincial department of education science and technology research project (B2016445).
Cite this paper
Zhou, S.S., Li, K.H., Tang, T.T. and Shi, D.P. (2017) Study on the Corrosion Inhibition Characteristic of ZH and ZG Mannich Base Inhibitors. Open Journal of Yangtze Gas and Oil, 2, 151-160. https://doi.org/10.4236/ojogas.2017.23011
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