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X65碳钢的H2S/CO2腐蚀控制因素研究
引用本文:陆原,赵景茂,张勇,张妙玮,刘言霞,程艳.X65碳钢的H2S/CO2腐蚀控制因素研究[J].北京化工大学学报(自然科学版),2021,48(3):17-25.
作者姓名:陆原  赵景茂  张勇  张妙玮  刘言霞  程艳
作者单位:1. 中海油(天津)油田化工有限公司, 天津 300450;2. 北京化工大学 材料科学与工程学院, 北京 100029
摘    要:目前,H2S/CO2腐蚀过程的控制因素判定依据主要参考Dunlop等的研究结果,但该判定结果经常与油田实际腐蚀情况不相符。为找到造成偏差的主要原因,更好地指导生产实践,采用动态高温高压釜,使用扫描电子显微镜(SEM)、能谱仪(EDS)和X射线衍射(XRD)等手段对X65碳钢在H2S/CO2共存体系中的腐蚀控制因素进行了研究。结果表明,不同温度下平均腐蚀速率随H2S/CO2分压比(pH2S/pCO2)的变化呈现两种不同的规律,这与腐蚀产物的膜形态和组成密切相关;腐蚀控制因素与pH2S/pCO2有关,而pH2S/pCO2临界值大小与温度密切相关。对于H2S腐蚀控制,当温度低于40℃时,Dunlop等的研究结果仍然适用;当温度从40℃升高至60℃时,本研究的pH2S/pCO2临界值由0.05升高到0.10。对于CO2腐蚀控制,本研究的pH2S/pCO2临界值在85℃以上时由原来的0.002逐渐升高到0.003。根据以上研究结果,修正了X65碳钢的H2S/CO2腐蚀过程的控制因素与pH2S/pCO2及体系温度的关系图。

关 键 词:H2S/CO2共存体系  腐蚀速率  腐蚀产物  控制因素  分压比  
收稿时间:2021-03-01

Factors controlling H2S/CO2 corrosion of X65 carbon steel
LU Yuan,ZHAO JingMao,ZHANG Yong,ZHANG MiaoWei,LIU YanXia,CHENG Yan.Factors controlling H2S/CO2 corrosion of X65 carbon steel[J].Journal of Beijing University of Chemical Technology,2021,48(3):17-25.
Authors:LU Yuan  ZHAO JingMao  ZHANG Yong  ZHANG MiaoWei  LIU YanXia  CHENG Yan
Affiliation:1. Cener Tech Oilfield Chemical Co., Ltd., Tianjin 300450;2. College of Materials Science and Engineering, Beijing University of Chemical Technology, Beijing 100029, China
Abstract:Corrosion control factors are mainly determined based on the results of Dunlop et al., but these are often inconsistent with the actual corrosion conditions in an oil field. In order to identify the main reasons for the deviations and better guide production practice, the factors controlling the corrosion of X65 carbon steel in an H2S/CO2 system were studied in a dynamic high temperature autoclave, using scanning electron microscopy (SEM), energy dispersive spectrometry (EDS) and X-ray diffraction (XRD). The results showed that the average corrosion rate varied with H2S/CO2 partial pressure ratio (pH2S/pCO2), displaying two different laws at different temperatures, which are closely related to the morphology and composition of the corrosion product film. The factors controlling corrosion are related to pH2S/pCO2, and the critical value of pH2S/pCO2 is closely related to the temperature. For H2S corrosion control, the results of Dunlop et al. are valid when the temperature is below 40 ℃. When the temperature was increased from 40 ℃ to 60 ℃ in this study, the critical value of pH2S/pCO2 increased from 0.05 to 0.10. For CO2 corrosion control, the critical value of pH2S/pCO2 gradually increased from 0.002 to 0.003 when the temperature exceeded 85 ℃. On the basis of the above results, the relationship between the factors controlling the H2S/CO2 corrosion process in X65 carbon steel and pH2S/pCO2 and system temperature can be reformulated.
Keywords:H2S/CO2 coexisting system  corrosion rate  corrosion products  controlling factors  partial pressure ratio  
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