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Premature Failure of API~((1)) 650 Oil Storage Tank Bottom Plates Due to Soil Side Corrosion

机译:由于土壤侧腐蚀而导致API〜((1))650储油罐底板过早失效

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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:炼油厂的地上储油罐(AST)经受着底板下侧(土壤)的腐蚀,异常高的速率为1毫米/年。自调试(2006-2015年)以来的9年内,这导致4辆坦克发生故障。腐蚀形态为严重的局部腐蚀,并带有大的深坑。 AST的底面腐蚀保护的设计是通过提供外加电流阴极保护(ICCP)系统(MMO网格阳极系统)来进行的。储罐最近和过去的阴极保护(CP)调查清楚地表明,储罐两端的极低(正电)极化电位表明CP系统自投运以来未正常运行。水的侵入(通过环形板和地基之间的缝隙)(主要是泄漏的消防水喷淋头)引入的水加剧了所观察到的腐蚀速率,这些消防喷淋头引入了细菌和腐蚀性阴离子,如氯离子和硫酸根。由于CP系统无效且无其他腐蚀控制手段,因此罐底在暴露于严重细菌和沉积物腐蚀的情况下,在调试后的8年内会穿孔并损失库存。已经采用了短期策略,由此腐蚀速率大大减慢,从而允许罐周转的分布尽可能长。气相抑制剂被用来暂时延长罐底板的寿命。从长远来看,炼油厂建议在现有CP设计基础上使用高电阻率的沥青砂混合料基础(不使用CP系统),这是基于20到30年沥青设计的无故障记录,该记录在该厂其他工厂的储罐中经历过公司。本文总结了观察结果,CP勘测的详细信息,测试,结果以及精炼厂采用的方法。

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