Investigation of the Corrosion Behavior of Mild Steel/H2SO4 Systems

被引:0
作者
Al-Moubaraki, A. H. [1 ]
Ganash, A. A. [2 ]
Al-Malwi, S. D. [2 ]
机构
[1] Univ AlJeddah, Fac Sci, Chem Dept, Alfaisaliah Campus, Jeddah, Saudi Arabia
[2] King Abdulaziz Univ, Fac Sci, Chem Dept, Jeddah, Saudi Arabia
来源
MOROCCAN JOURNAL OF CHEMISTRY | 2020年 / 8卷 / 01期
关键词
Corrosion; Sulfuric acid; Mild steel; pits; anodic control; SO42-; anions; ANODIC-DISSOLUTION; STEEL; IRON; INHIBITION; MECHANISM; ALLOY; AL;
D O I
暂无
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The corrosion behavior and mechanism of mild steel/H2SO4 systems were examined using hydrogen gas evolution, HE, and weight loss, WL, as chemical measurements and electrochemical impedance spectroscopy, EIS, and potentiodynamic polarization, PDP, as electrochemical measurements at 30 degrees C. From the chemical results, the corrosion rate of mild steel increased as well as increasing acid concentration, with a reaction constant of 0.70 and 0.60 for HE and WL, respectively. Different features including general and pitting corrosion can be shown on the mild steel surface after dipping in different concentrations of H2SO4, and the latter became more distinct at higher acid concentrations. EIS results showed that the R-p value decreases while the C-dl value increases along with increasing acid concentration. PDP results clearly revealed that the dissolution of mild steel undergoes anodic control. The chemical and electrochemical method suggested that the dissolution mechanism of mild steel is the same at different H2SO4 concentrations. Based on the results and observations, the mechanism of mild steel corrosion in H2SO4 can be explained based on the role of SO42- anions, the main corrosive agent in aqueous H2SO4 solutions, which partake directly in anodic dissolution and cathodic reaction during corrosion.
引用
收藏
页码:264 / 279
页数:16
相关论文
共 37 条
[11]   Phenothiazine as inhibitor of the corrosion of cadmium in acidic solutions [J].
ElSayed, A .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1997, 27 (02) :193-200
[12]  
FERHAT Mahmoud., 2014, Journal of Materials and Environmental Science, V5, P1059
[13]   EFFECT OF VELOCITY AND OXYGEN ON CORROSION OF IRON IN SULFURIC ACID [J].
FOROULIS, ZA ;
UHLIG, HH .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1964, 111 (01) :13-17
[14]   A MATHEMATICAL-MODEL FOR THE CORROSION OF IRON IN SULFURIC-ACID [J].
GAN, EC ;
ORAZEM, ME .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1987, 134 (06) :1357-1366
[15]  
Hines J.G., 1964, CORROS SCI, V4, P201, DOI 10.1016/0010-938X(64)90019-8
[16]  
Lyon S, 2012, WOODHEAD PUBL SER EN, P3
[17]   THE DISSOLUTION MECHANISM OF IRON IN CHLORIDE SOLUTIONS [J].
MACFARLANE, DR ;
SMEDLEY, SI .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1986, 133 (11) :2240-2244
[18]   REACTION-RATE STUDIES FOR THE CORROSION OF METALS IN ACIDS .1. IRON IN MINERAL ACIDS [J].
MATHUR, PB ;
VASUDEVAN, T .
CORROSION, 1982, 38 (03) :171-178
[19]  
Mindyuk A.K., 1967, FIZ KHIM MEKH MATER, V3, P157
[20]   EFFECT OF SULFURIC-ACID CONCENTRATION ON THE RATE OF TRIBOCORROSION OF IRON [J].
MISCHLER, S ;
ROSSET, E ;
STACHOWIAK, GW ;
LANDOLT, D .
WEAR, 1993, 167 (02) :101-108