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Premature Failure of API 650 Oil Storage Tank Bottom Plates Due to Soil Side Corrosion

机译:API 650储油罐底板的过早损坏由于土壤侧腐蚀

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The above ground storage tanks (AST's) in the refinery is experiencing bottom plate underside (soil) corrosion at an extraordinarily high rate of 1 mm/year. This has resulted in the failure of 4 tanks within a period of 9 years since commissioning (2006-2015). The corrosion morphology is of severe localized corrosion with large deep pits. The design of the underside corrosion protection for the AST's is by providing an impressed current cathodic protection (ICCP) system (MMO grid anode system). Recent and past cathodic protection (CP) survey of the tanks clearly reveal a very low (electropositive) polarized potential across the tanks indicating the CP system has not functioned correctly since commissioning. The corrosion rates observed has been amplified by the ingress of water (through the gaps between annular plate and foundation), primarily from leaking fire water sprinklers, which bring in bacteria and corrosive anions like chloride and sulfate. With the CP system being ineffective and no other means of corrosion control, the tank floor was exposed to a severe form of bacterial and under deposit corrosion leading to perforation and loss of inventory within 8 years from commissioning. A short term stratagem has been employed whereby the corrosion rate was substantially slowed thus permitting distribution of the tank turnarounds across as many years as possible. Vapor phase inhibitors were used to temporarily extend the life of the tank bottom plates. For the long term, the refinery recommends a high resistivity bitumen sand mix foundation (without CP system) over the existing CP design based on trouble free track record of 20-30 years of the bitumen design that was experienced in tanks of other plants within the company. The article summarizes the observations, details of the CP survey, tests, results and forward path taken up by the refinery.
机译:炼油厂的上述地面储罐(AST)正在经历底板下侧(土壤)腐蚀,以1毫米/年的速度非常高。这导致4个坦克在调试后的9年内失败(2006 - 2015年)。腐蚀形态具有严重的局部腐蚀,具有大的深坑。 AST对AST的下侧腐蚀保护的设计是通过提供一个深刻的电流阴极保护(ICCP)系统(MMO网格阳极系统)。最近和过去的阴极保护(CP)坦克的调查清楚地揭示了在坦克上的非常低(电动)极化潜力,这表明CP系统自调试以来已经无法正常运行。观察到的腐蚀速率由水的进入(通过环形板和基础之间的间隙)扩增,主要来自泄漏的火水喷水器,它引入氯化物和硫酸盐等细菌和腐蚀性阴离子。随着CP系统无效,没有其他腐蚀控制的手段,罐地板暴露于严重的细菌和沉积腐蚀,导致在8年内从调试后8年内穿孔和损失。已经采用短期策略,从而腐蚀速率显着放缓,从而允许尽可能多岁的罐变性分布。使用气相抑制剂暂时延长罐底板的寿命。从长远来看,炼油厂在现有的CP设计上推荐高电阻率沥青砂基础(没有CP系统),基于现有的CP设计,基于沥青设计的故障轨迹记录在其他植物中的沥青设计中的沥青设计中的零售公司。本文总结了意见,CP调查,测试,结果和前进路径的详细信息。

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