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Failure analysis: SCC limits of AISI 321 stainless steel grade for oil gas

机译:失效分析:针对石油和天然气的AISI 321不锈钢牌号的SCC限制

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While AISI 321 should not be used in offshore environment anymore, a production separator made of AISI 321 was used on a Total E&P asset in the Middle East for more than 20 years of service in presence of salts, CO_2 and H_2S at about 60°C; Recently, the process temperature raised to 70-75°C causing a severe cracking and leakage. The crack occurred close to the vessel inlet where both the temperature and the chloride content are very high (T=70-75°C and about of 150,000 g/1 Cl~-). In addition, at the crack location the calculated pH at 60-70°C range is above 5, as this location is close to liquid entrance and the presence of formation water is very likely. On the other hand, no crack was detected at the other extremity of the vessel where the temperature is around 60°C. The chloride content would be low on top of the vessel in contact with the gas phase. Due to condensation effects at this location, the estimated pH can be lower than 4 and CT concentration down to 1000 ppm. In this context, this paper deals with some laboratory tests in order to determine the threshold temperature for SCC initiation on AISI 321 alloy under high chloride concentration in formation and condensed water conditions and in presence of H_2S.
机译:虽然AISI 321不应再用于海上环境,但在大约60°C的盐,CO_2和H_2S存在的情况下,由AISI 321制成的生产分离器已在中东的Total E&P资产上使用了20多年;最近,工艺温度升至70-75°C,导致严重的开裂和泄漏。裂纹发生在靠近容器入口处,温度和氯化物含量都很高(T = 70-75°C,约为150,000 g / 1 Cl〜-)。此外,在裂纹位置,计算出的60-70°C范围内的pH值高于5,因为该位置靠近液体入口,并且很可能存在地层水。另一方面,在温度为60℃左右的容器的另一端没有发现裂纹。与气相接触的容器顶部的氯化物含量较低。由于该位置的凝结效应,估计的pH值可能低于4,CT浓度低至1000 ppm。在这种情况下,本文进行了一些实验室测试,以确定在地层和冷凝水条件下高氯化物浓度和H_2S存在下AISI 321合金上SCC引发的阈值温度。

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