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首页> 外文期刊>Journal of Failure Analysis and Prevention >Assessment of Corrosion Damage in a Finger-Type Slug Catcher
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Assessment of Corrosion Damage in a Finger-Type Slug Catcher

机译:手指型Sl式捕手的腐蚀损伤评估

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Corrosion pits of up to 6 mm depth, associated with areas of high solid deposition were discovered in the finger-type slug catcher and glycol sump during routine inspection (first in 2005 and then in 2013) following lengthy periods of below-threshold CI injection and partial implementation of the corrosion management plan. Corrosion rates were predicted to have increased from 0.46 mm/year in 2005 to 0.71 mm/year in 2007 and then decreased to 0.41 mm/year in 2008. Subsequent integrity assessments concluded that the slug catcher was not fit for continued operation at the current rate of pitting and was therefore shut down to prevent potential loss of containment. Results of API 579 fitness for service assessments of the corroded areas justified the subsequent decision to de-rate the system and that no further corrosion can be tolerated at the original design pressure, at least until the rates of corrosion and its mechanisms were fully understood. Based on the damage morphology, chemical and monitoring data and theoretical concepts, a synergy of mechanisms (under deposit corrosion, CO_2 corrosion, preferential weld corrosion and microbial-induced corrosion) is identified as being responsible for the observed damage. The short-term mitigation plan is to routinely inspect the damaged locations (by UT wall thickness checks) while simultaneously implementing a corrosion management and control plan which consists of: continuous inhibitor dosing, pH stabilisation (with MEA/DEA) to above pH 6, batch biociding, sampling of residuals, chlorides, iron, SRB/GHB count, water cut, water content and pH of lean glycol, glycol content of pipeline fluid and online monitoring. The inspection, sampling and monitoring results should then be reviewed initially monthly, subsequently quarterly by the corrosion and integrity team in order to assess the rate of pitting. If the target (<0.125 mm/year) is being breached frequently, then alternative but more costly mitigation should be considered such as repair or outright replacement of the finger-type by vessel-type slug catchers which have built-in sand jetting systems designed to deal with high deposition rates and are therefore considered less prone to associated corrosion damage.
机译:在长时间的低于阈值注入CI和之后的例行检查期间(首先在2005年,然后在2013年),在手指式塞子捕集器和乙二醇池中发现了深度高达6 mm的腐蚀坑,并伴有高固体沉积区域。部分执行腐蚀管理计划。腐蚀率预计将从2005年的0.46 mm /年增加到2007年的0.71 mm /年,然后在2008年下降到0.41 mm /年。随后的完整性评估得出的结论是,塞块捕集器不适合以当前的速率继续运行点蚀,因此被关闭以防止潜在的密闭性损失。 API 579适用于腐蚀区域的服务评估的结果证明了随后决定降低系统额定值的理由,并且在最初的设计压力下不能容忍进一步的腐蚀,至少直到完全了解腐蚀速率及其机理为止。根据损伤形态,化学和监测数据以及理论概念,可以确定机理的协同作用(在沉积物腐蚀,CO_2腐蚀,优先焊接腐蚀和微生物引起的腐蚀下)是造成观察到的破坏的原因。短期缓解计划是例行检查损坏的位置(通过UT壁厚检查),同时实施腐蚀管理和控制计划,其中包括:连续添加抑制剂,pH稳定(使用MEA / DEA)至pH大于6,分批杀菌,残留物采样,氯化物,铁,SRB / GHB计数,含水率,稀乙二醇的水含量和pH值,管道液中乙二醇的含量以及在线监控。然后应首先每月检查检查,采样和监测结果,然后由腐蚀和完整性团队每季度检查一次,以评估点蚀率。如果经常违反目标(<0.125毫米/年),则应考虑采取替代措施,但成本更高的缓解措施,例如用内置式喷砂系统的船用塞子捕集器对指型进行修理或更换。处理高沉积速率,因此被认为较不容易受到相关的腐蚀破坏。

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