郭超, 俞龙, 赵泽茂, 谢灿波. 南苏丹法罗杰FPF站场气相腐蚀分析及对策[J]. 油气储运, 2018, 37(5): 527-532. DOI: 10.6047/j.issn.1000-8241.2018.05.008
引用本文: 郭超, 俞龙, 赵泽茂, 谢灿波. 南苏丹法罗杰FPF站场气相腐蚀分析及对策[J]. 油气储运, 2018, 37(5): 527-532. DOI: 10.6047/j.issn.1000-8241.2018.05.008
GUO Chao, YU Long, ZHAO Zemao, XIE Canbo. Factor analysis and countermeasures of gas corrosion at Palouch FPF station in the South Sudan[J]. Oil & Gas Storage and Transportation, 2018, 37(5): 527-532. DOI: 10.6047/j.issn.1000-8241.2018.05.008
Citation: GUO Chao, YU Long, ZHAO Zemao, XIE Canbo. Factor analysis and countermeasures of gas corrosion at Palouch FPF station in the South Sudan[J]. Oil & Gas Storage and Transportation, 2018, 37(5): 527-532. DOI: 10.6047/j.issn.1000-8241.2018.05.008

南苏丹法罗杰FPF站场气相腐蚀分析及对策

Factor analysis and countermeasures of gas corrosion at Palouch FPF station in the South Sudan

  • 摘要: 为了给南苏丹法罗杰FPF站场扩建项目的气相选材和防腐设计提供理论依据, 对该站原油伴生气腐蚀进行了研究。利用2005年NORSOK M-506“CO2腐蚀速率计算模型”中关于CO2气相腐蚀的计算方法, 研究了系统压力、水相pH值、温度、壁面剪切力等参数对法罗杰FPF站场原油伴生气腐蚀性的影响。结果表明: 在该项目伴生气参数的变化区间, 压力和水相pH值对伴生气腐蚀性影响显著, 随着压力的升高和水相pH值的降低, 伴生气腐蚀性急剧增强; 随着温度的升高, 伴生气腐蚀性先逐步增强, 在40~80℃达到某一最大值后又逐步降低; 壁面剪切力的增加也导致伴生气腐蚀性增强, 但相比其他因素, 壁面剪切力对伴生气腐蚀性变化的影响较小, 据此推荐了CO2腐蚀的控制措施。

     

    Abstract: In this paper, the corrosion of oil associated gas at Palouch FPF station in the South Sudan was analyzed to provide the theoretical basis for gas material selection and corrosion prevention design of its expansion project. The effects of system pressure, water-phase pH value, temperature and wall shear stress on the corrosion of oil associated gas at Palouch FPF station were studied by using the CO2 corrosion calculation method described in "Calculation Model of CO2 Corrosion Rate"(NORSOK M-506, 2005). It is indicated that in the change interval of associated gas parameters of this project, associated gas corrosion is significantly affected by pressure and water-phase pH value, and it increases sharply with the increase of pressure and the decrease of water-phase pH value. As the temperature rises, associated gas corrosion increases gradually and then decreases gradually after it reaches the peak value in the range of 40-80 ℃. Associated gas corrosion is also increased with the increase of wall shear stress, but compared with other factors, wall shear stress has less effect on the change of associated gas corrosion. And accordingly the countermeasures to prevent CO2 corrosion were recommended.

     

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