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首页> 外文期刊>Corrosion >Investigation of the Galvanic Mechanism for Localized Carbon Dioxide Corrosion Propagation Using the Artificial Pit Technique
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Investigation of the Galvanic Mechanism for Localized Carbon Dioxide Corrosion Propagation Using the Artificial Pit Technique

机译:用人工坑技术研究局部二氧化碳腐蚀传播的电机制

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摘要

Localized carbon dioxide (CO2) corrosion is the most dangerous type of internal corrosion to mild steel pipelines in the oil and gas industry since the penetration rate of localized corrosion can be one or more magnitudes higher than that of uniform corrosion. In this study, the focus is on propagation of localized CO2 corrosion on mild steel that occurs by a galvanic mechanism. A galvanic cell is established by the coupling of two distinct areas in a conductive CO2 solution: a bare steel surface and an iron carbonate (FeCO^sub 3^) layer-covered steel surface. It was found that localized CO2 corrosion propagates when a stable difference in corrosion potential is established between the anode (bare steel surface) and the cathode (FeCO^sub 3^-covered surface). Stable propagation will occur only when the conditions are in the "gray zone," i.e., close to saturation with respect to FeCO^sub 3^, when no significant FeCO^sub 3^ dissolution nor precipitation is expected. Practically, this corresponds to when FeCO^sub 3^ supersaturation (SS^sub FeCO^sub 3^^) is in the range from 0.5 to 2. The key environmental factors that affect propagation of localized CO2 corrosion of mild steel are temperature, pH, partial pressure of CO2, salt concentration, and flow velocity. A protective FeCO^sub 3^ layer forms at high temperature (>50° C); therefore, the galvanic mechanism of localized corrosion is valid only in this range. pH needs to be such that moderately protective FeCO^sub 3^ layers form, typically at pH 5.5 to 6.5. Critical partial pressures of CO2 is around 0.1 bar to 2 bar, above this very protective FeCO^sub 3^ films form at high temperature, giving a very low likelihood of localized attack. The solubility of FeCO^sub 3^ increases with increasing salt concentration, making it more difficult to form protective FeCO^sub 3^ layers and more likely to get localized corrosion propagation. Turbulent flow assists localized corrosion propagation by sweeping away corrosion products from the rapidly corroding steel surface and thereby preventing reformation of the protective FeCO^sub 3^ layer. [PUBLICATION ABSTRACT]
机译:局部二氧化碳(CO2)腐蚀是石油和天然气行业中低碳钢管道最危险的内部腐蚀类型,因为局部腐蚀的渗透率可能比均匀腐蚀的渗透率高一个或多个数量级。在这项研究中,重点是通过电化机理在低碳钢上传播局部CO2腐蚀。通过在导电性CO2溶液中两个不同区域的耦合来建立原电池,这两个区域分别是裸露的钢表面和覆盖有碳酸铁(FeCO 3 3)层的钢表面。发现当在阳极(裸钢表面)和阴极(FeCO 2覆盖3 ^的表面)之间建立稳定的腐蚀电位差时,局部CO 2腐蚀扩散。仅当条件处于“灰色区域”,即相对于FeCO 3接近饱和时,并且预期没有明显的FeCO 3溶解或沉淀时,才会发生稳定的传播。实际上,这对应于FeCO 2亚超饱和度(SS 3亚FeCO 3摩尔)的范围为0.5到2。影响低碳钢局部CO2腐蚀传播的关键环境因素是温度,pH ,CO2分压,盐浓度和流速。在高温(> 50°C)下会形成一层保护性的FeCO 2 sub 3层。因此,局部腐蚀的电机制仅在此范围内有效。 pH需要使得通常在pH 5.5至6.5下形成适度保护的FeCO 3层。 CO 2的临界分压约为0.1 bar至2 bar,高于在高温下形成的这种非常保护性的FeCO 2 3 x膜,因此发生局部侵蚀的可能性非常低。 FeCO 2 3 3的溶解度随着盐浓度的增加而增加,使得形成保护性FeCO 3 3层更加困难,并且更可能发生局部腐蚀扩展。湍流通过从快速腐蚀的钢表面清除腐蚀产物而有助于局部腐蚀的传播,从而防止保护性FeCO 2 3 3层的再形成。 [出版物摘要]

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  • 来源
    《Corrosion》 |2010年第9期|p.1-12|共12页
  • 作者

    J Han B N Brown S Nesic;

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    J. Han, * B. N. Brown,** and S. Nesic[double dagger],**Submitted for publication May 20, 2009: in revised form. May 13, 20 10. Part of this paper was presented as paper no. 07323 at CORROSION/2007. March 2007, Nashville. TN.[double dagger] Corresponding author. E-mail: nesic@ohio.edu.* Institute for Corrosion and Multiphase Technology, Department of Chemical and Biomolecular Engineering, Ohio University. 342 West State St.. Athens. OH 45701. Present address: Earth Systems Observations (EES- 14), Earth and Environmental Sciences Division (EES). Los Alamos National Laboratory. Los Alamos, NM.** Institute for Corrosion and Multiphase Technology, Department of Chemical and Biomolecular Engineering. Ohio University. 342 West State St., Athens, OH 45701.;

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