首页> 外文会议>Annual Conference and Exposition on Corrosion NACExpo >INVESTIGATION OF A CORROSION FAILURE IN AN OFFSHORE GAS COMPRESSION SYSTEM: THE ROLE OF H2S SCAVENGER AND ORGANIC ACIDS
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INVESTIGATION OF A CORROSION FAILURE IN AN OFFSHORE GAS COMPRESSION SYSTEM: THE ROLE OF H2S SCAVENGER AND ORGANIC ACIDS

机译:海上气体压缩系统中腐蚀衰竭的研究:H2S清除剂和有机酸的作用

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A corrosion failure was experienced in the gas compression module of the Gorm C platform in the Danish sector of the North Sea. It was found that the carbon steel discharge pipe from IP compressor A had ruptured causing gas to leak to the module. This paper describes the subsequent investigation into the corrosion mechanism responsible. The pattern of corrosion seen in the ruptured Gorm C pipe shows clearly that the corrosion is related to the injection of H_2S scavenger into the dry gas phase, 5 percent relative humidity (RH) at 135 deg C. The corrosion attack is seen as a gradual increase in metal loss from just downstream of the scavenger injection point to the point of rupture immediately after the first bend. The metal loss is seen where a continuous phase of liquid scavenger is expected to be present. Corrosion tests carried out on the commercial scavenger product containing the active component 1,3,5-tri(2-hydroxyethyl)-(2H,4H,6H)- hexahydro-1,3,5-Triazine show clearly that the corrosivity as a function of temperature increases dramatically at a temperature of 80-100 deg C. This is attributed to a thermal breakdown of the product reverting to the reactants of formaldehyde and monoethanolamine (MEA), and, in turn, in the formation of formic acid, which reacts with MEA to form the salt. This is supported by the finding of ester /carboxylic acid, proportional to the metal loss, in the surface layer of the pipe. Inclusion of CO_2 in the corrosion tests results in a further increase in corrosivity, probably due to the absence of a protective iron carbonate layer that would be expected to form on carbon steel in the presence of CO_2 at the given test conditions.
机译:北海丹麦地板的GOM型平台的气体压缩模块中经历了腐蚀性故障。发现来自IP压缩机A的碳钢排放管道已经破裂导致气体泄漏到模块上。本文介绍了随后的腐蚀机制调查。破裂的GORM C管中所见的腐蚀模式清楚地表明,腐蚀与将H_2S清除剂注射到干气相中,在135℃下的5%相对湿度(RH)。腐蚀攻击被视为渐变在第一次弯曲后立即从清除剂注射点的下游增加金属损失。期望预期液体清除剂的连续相位存在金属损失。在含有活性组分1,3,5-Tri(2-羟乙基) - (2H,4H,6H) - 六羟基-1,3,5-三嗪的商业清除剂产品上进行的腐蚀试验显然显示腐蚀性温度的功能在80-100℃的温度下显着增加。这归因于产品的热分解,该产品恢复到甲醛和单乙醇胺(MEA)的反应物中,并且反过来,在形成甲酸中的形成与MEA反应形成盐。通过在管道的表面层中找到与金属损耗成比例的酯/羧酸的发现。在腐蚀试验中包含CO_2导致腐蚀性的进一步增加,这可能是由于在给定的试验条件下在CO_2存在下预期在碳钢上形成的保护铁碳酸盐层。

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