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Metal dusting in the low-point drains of crossover piping system in petrochemical environment

机译:石化环境中交叉管道系统低位排水口的金属粉尘

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In April, 2008, a leak from a welded elbow was found on the coil inlet piping of an ethane cracking furnace in one of NOVA Chemicals plants. Subsequent examinations identified more potential failure locations, e.g. abandoned thermowells, low-point drains. All these locations were identified as containing confined spaces, which were relatively isolated from the process stream and allowed the buildup of coke. Extensive analysis revealed that metal dusting of the 304H stainless steel was responsible for the material wastage and reduction of wall thickness at these specific locations. This paper describes the analysis on the low-point drains and elaborates on the corresponding mechanism of the metal dusting in these confined spaces. Two 304H stainless steel (SS) low-point drains were analyzed to investigate the root causes of the failure. These failed low-point drains were located in the crossover piping system of an ethane cracking furnace. The failure was in the form of material loss, resulting in the thinning of the plug wall and creating a leak path. The analysis confirmed that the material loss was the result of metal dusting due to excessive carbon deposition and carburization. The metal dusting is proposed to occur in the decoking process, which is an oxidizing environment, rather than the cracking process. Excessive carbon content was detected in the void formed by metal dusting and the crevice between the threads. The coke formation was in the form of catalytic coking, promoted by the existing catalysts (iron and/or nickel) in 304H SS. The metallurgical analysis revealed carburization in the steel and local burns were present simultaneously with the metal dusting. The reduction or disappearance of the original protective layer (Cr_2O_3) allowed a diffusion path of the carbonaceous gases, thus creating carburization and metal dusting. The disappearance of the protective oxide (Cr_2O_3) layer was the result of local excessive temperature causing loss of chromium.
机译:2008年4月,在NOVA Chemicals一家工厂的乙烷裂化炉的盘管入口管道上发现了焊接弯头的泄漏。随后的检查确定了更多潜在的故障位置,例如废弃的热套管,低位排水管。所有这些位置均被确定为包含密闭空间,这些密闭空间与工艺流相对隔离,并允许积聚焦炭。广泛的分析表明,在这些特定位置,304H不锈钢的金属喷粉是造成材料浪费和壁厚减小的原因。本文描述了低点排水的分析,并阐述了这些密闭空间中金属粉尘的相应机理。分析了两个304H不锈钢(SS)低点排放口,以调查故障的根本原因。这些不合格的低点排水管位于乙烷裂解炉的交叉管道系统中。失效形式为材料损失,导致塞壁变薄并形成泄漏路径。分析证实,材料损失是由于过多的碳沉积和渗碳导致的金属粉尘的结果。提出金属粉尘发生在除氧化过程的焦化过程中,而不是裂化过程。在金属粉尘和螺纹之间的缝隙形成的空隙中检测到过多的碳含量。 304H SS中现有的催化剂(铁和/或镍)促进了焦炭形成的催化焦化形式。冶金分析表明,钢中渗碳,金属粉尘同时存在局部烧伤。原始保护层(Cr_2O_3)的减少或消失允许碳质气体的扩散路径,从而产生渗碳和金属粉尘。保护性氧化物(Cr_2O_3)层的消失是局部高温导致铬损失的结果。

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