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中国腐蚀与防护学报  2026, Vol. 46 Issue (5): 1537-1548     CSTR: 32134.14.1005.4537.2025.373      DOI: 10.11902/1005.4537.2025.373
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23MnNiMoCr54钢在不同pH的模拟高矿化水中腐蚀机理研究
曹天慧1, 杨砚淇2, 刘雨薇2, 吴磊2, 郭泉忠2, 贾志刚2, 曹公望2(), 汪川2()
1.沈阳化工大学材料科学与工程学院 沈阳 110142
2.中国科学院金属研究所 辽宁沈阳土壤大气环境材料腐蚀国家野外科学观测研究站 沈阳 110016
Corrosion Behavior of 23MnNiMoCr54 Steel in Artificial High-mineralized Mine Waters of Different pH Values
CAO Tianhui1, YANG Yanqi2, LIU Yuwei2, WU Lei2, GUO Quanzhong2, JIA Zhigang2, CAO Gongwang2(), WANG Chuan2()
1.School of Materials Science and Engineering, Shenyang University of Chemical Technology, Shenyang 110142, China
2.National Field Scientific Observation and Research Station of Soil and Atmospheric Environmental Material Corrosion in Shenyang, Institute of Metal Research, Chinese Academy of Sciences, Shenyang 110016, China
引用本文:

曹天慧, 杨砚淇, 刘雨薇, 吴磊, 郭泉忠, 贾志刚, 曹公望, 汪川. 23MnNiMoCr54钢在不同pH的模拟高矿化水中腐蚀机理研究[J]. 中国腐蚀与防护学报, 2026, 46(5): 1537-1548.
Tianhui CAO, Yanqi YANG, Yuwei LIU, Lei WU, Quanzhong GUO, Zhigang JIA, Gongwang CAO, Chuan WANG. Corrosion Behavior of 23MnNiMoCr54 Steel in Artificial High-mineralized Mine Waters of Different pH Values[J]. Journal of Chinese Society for Corrosion and protection, 2026, 46(5): 1537-1548.

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摘要: 

研究了23MnNiMoCr54钢(54钢)在pH = 5、8和9的模拟高矿化水中的腐蚀行为,阐述不同pH值高矿化水引发的54钢腐蚀行为的差异性。选用腐蚀介质是矿化度为10 g/L的模拟矿化水,并依据依我国典型矿区井下水的实际情况,配制了3种同质但pH值不同(pH = 5、8和9)的模拟矿化水,采用X射线衍射、扫描电子显微镜及电化学测试等手段,分析54钢的腐蚀产物组成、表面形貌及电化学行为演变。结果表明,在高矿化度水中腐蚀性离子(Cl-、SO42-)的侵蚀作用与pH影响的产物层结构演变,是影响54钢腐蚀失效的核心因素。弱碱性高矿化度水有利于钢表面稳定防护层的生成,酸性水则加速腐蚀失效。研究结果可为不同pH特征矿区的54钢防腐设计提供科学依据。

关键词 : 23MnNiMoCr54钢,  高矿化水,  pH,  腐蚀产物,  电化学    
Abstract:

In order to address the issue that the steel used in mining engineering in mining areas around the country is prone to failure due to corrosion caused by the high mineral containing mine waters with varying pH values. Herein, the corrosion behavior of 23MnNiMoCr54 steel in artificial high-mineralized mine waters with pH values of 5, 8, and 9 respectively was studied by means of immersion test, thickness loss measurement, X-ray diffraction, scanning electron microscopy, and electrochemical tests etc in terms of the surface morphology, composition of corrosion products and evolution of electrochemical behavior of the steel. The corrosive medium selected was an artificial mineralized water with a mineralization degree of 10 g/L as precursor, then based on the actual situation of underground waters in typical mining areas around the country, three homogeneous but with different pH values (pH = 5, 8, and 9) of artificial mineralized waters were prepared. Results show that after immersion in the three high-mineralized mine waters respectively, the corrosion products of the steel were mainly composed of α-FeOOH, γ-FeOOH, β-FeOOH, and Fe3O4. Additionally, CaCO3 and Mg(OH)2 were generated in neutral and weakly alkaline waters, while a higher content of calcium/magnesium-containing products may form in the weakly alkaline water. The corrosion kinetic characteristics followed the trend of "initial increase in corrosion rate, subsequent decrease in the middle stage, and stabilization in the late stage". In acidic high-mineralized mine water, the corrosion rate was consistently higher than that in neutral and weakly alkaline waters due to the incomplete and easily soluble products scale. In the weakly alkaline water, Fe3O4 synergistically formed a compact products scale with CaCO3 and Mg(OH)2, exhibiting the optimal corrosion inhibition effect, while the corrosion rate in the neutral water was intermediate between the other two. High-mineralized mine water exerted dual effects: on one hand, high concentrations of Cl- and SO42- accelerated matrix dissolution and product scale damage; on the other hand, it induced the enrichment of CaCO3 and Mg(OH)2 on the outer portion of rust scale in neutral and weakly alkaline waters, indirectly promoting the formation of a composite protective produts scale. The corrosive effect of aggressive ions (Cl-, SO42-) in high-mineralized mine water and the pH-dependent structural evolution of the products scales are the core factors affecting the corrosion failure of the steel. The weakly alkaline water is conducive to the formation of a stable protective scale, whereas the acidic water may accelerate the corrosion failure. This study provides a scientific basis for the corrosion protection design for steels such as 23MnNiMoCr54 steel used in mining areas with different pH characteristics.

Key words: 23MnNiMoCr54 steel    high-mineralized mine water    pH    corrosion product    electrochemistry
收稿日期: 2025-12-11      32134.14.1005.4537.2025.373
ZTFLH:  TG174.4  
基金资助:广州市重点研发计划(2024B01J0037);中国博士后科学基金(2025M770152)
通讯作者: 汪川,E-mail:cwang@imr.ac.cn,研究方向为腐蚀科学与防护;
曹公望,E-mail:gwcao@imr.ac.cn,研究方向为材料自然环境腐蚀
Corresponding author: WANG Chuan, E-mail: cwang@imr.ac.cn;
CAO Gongwang, E-mail: gwcao@imr.ac.cn
作者简介: 曹天慧,男,1997年生,硕士生
ParameterpHTDS / mg·L-1
Eastern5.0-8.5500-2000
Central6.8-8.51500-3000
Western8.0-9.1> 3000
表1  我国典型矿区腐蚀环境
SolutionNaHCO3MgSO4CaSO4·2H2ONaClNa2SO4TDS
pH 50.35 ± 0.050.5 ± 0.12 ± 0.10.3 ± 0.057 ± 0.19.9136
pH 80.35 ± 0.050.5 ± 0.12 ± 0.10.3 ± 0.057 ± 0.19.6028
pH 90.35 ± 0.050.5 ± 0.12 ± 0.10.3 ± 0.057 ± 0.19.6376
表2  高矿化水实验溶液配置 (g/L)
图1  54钢在不同pH的高矿化水中的腐蚀厚度损失和腐蚀速率随浸泡时间的变化
图2  54钢在不同pH的高矿化水中的浸泡后的XRD图谱
图3  54钢在不同pH的高矿化水中浸泡后的宏观形貌
图4  54钢在不同pH的高矿化水中浸泡后的SEM表面形貌
PointsFeCaMgSClCuCrNi
A89.720.871.512.710.472.021.191.51
B89.730.861.520.800.901.691.473.03
C82.900.270.492.590.451.525.835.95
D74.210.290.924.610.83.077.218.89
E86.95.501.311.410.161.830.782.11
F81.59.231.982.240.281.690.72.38
G74.8216.762.341.330.201.840.951.76
H71.5817.893.541.49-2.760.52.24
I82.278.043.681.19-1.630.942.25
J50.4637.406.152.10-1.460.651.78
K23.9158.2213.091.13-1.600.71.35
L3.1683.453.980.92-4.271.322.90
表3  图4中A~L标记的EDS元素组成 (atomic fraction / %)
图5  54钢在不同pH的高矿化水中浸泡后的SEM截面形貌
图6  54钢在不同pH的高矿化水中浸泡32 d截面形貌的EDS面扫描结果
图7  54钢在不同pH的高矿化水中浸泡不同时间的极化曲线
SolutionEcorr / VIcorr / μA·cm-2
4 d8 d16 d32 d4 d8 d16 d32 d
pH 5-0.685-0.770-0.711-0.72233.25644.49226.38414.553
pH 8-0.620-0.692-0.689-0.67029.47335.69524.83212.379
pH 9-0.660-0.593-0.677-0.62415.39424.9119.8018.401
表4  图7极化曲线拟合结果
图8  54钢在不同pH的高矿化水中浸泡不同时间的EIS谱
图9  用于EIS拟合的等效电路
SolutionTime / dRs / Ω⋅cm2QrRr / Ω⋅cm2QdlRct / Ω⋅cm2Rp / Ω⋅cm2
Yr / Ω-1⋅cm-2⋅S nnrYdl / Ω-1⋅cm-2⋅S nndl
pH 54175.410.76 × 10-3523.4 × 10-3633.59.482 × 10-3603.1 × 10-333.47666.97
8175.8301.6 × 10-3978.5 × 10-3354.49.025 × 10-3594.3 × 10-312.86367.26
16175.121.21 × 10-3409.5 × 10-3562.423.21 × 10-3762.2 × 10-3155.8718.2
32168.63.672 × 10-3735.9 × 10-3735.11.195 × 10-3760.0 × 10-3192.8927.9
pH 84167.2150.1 × 10-3637.4 × 10-3581.13.095 × 10-3636.6 × 10-391.94673.04
8167.518.58 × 10-3550.4 × 10-3400.07.670 × 10-3607.1 × 10-36.979406.979
16175.843.38 × 10-3372.6 × 10-3834.82.529 × 10-3627.0 × 10-328.44863.24
32179.13.586 × 10-3746.7 × 10-311774.608 × 10-3536.3 × 10-3517.81694.8
pH 94166.121.11 × 10-3937.4 × 10-3748.93.571 × 10-3612.9 × 10-330.41779.31
8174.512.22 × 10-3546.9 × 10-3676.28.259 × 10-3559.2 × 10-316.92693.12
16177.12.123 × 10-3635.2 × 10-3824.3362.7 × 10-6662.6 × 10-3151.1975.4
32179.52.502 × 10-3681.4 × 10-3153910.16 × 10-3454.2 × 10-3970.82509.8
表5  采用等效电路对EIS谱进行拟合得到的数据
图10  54钢在不同pH的高矿化水中的腐蚀产物层电阻、电荷转移电阻和极化电阻
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