适用于多相气凝析液输送的混合式管道

Nur Izyan Mukhtar, M. H. A Razak, Z. Jamil
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引用次数: 0

摘要

在正常和异常操作条件下,腐蚀和材料降解因素是评估海上管道输送处理过的气体和含有污染物(如CO2)的冷凝水的材料适用性的基本标准之一,符合ISO 15156要求的耐湿H2S损坏的材料和汞。根据ISO 15156的要求,在某些瞬态情况下,由于管道沿线有大量耐湿H2S损坏的材料,因此进行了全面的研究,以确定管道部分将暴露在酸性条件下。该研究是针对适合目的的解决方案和项目的资本支出优化计划进行的。在某些瞬态情况下,对于一定长度的管道,在潮湿条件下可能会暴露在大量的H2S中,这增加了材料对湿H2S损伤的敏感性,例如氢致开裂(HIC)/逐步开裂(SWC)和硫化物应力开裂(SSC)。使用组合跟踪模块的流动保证建模来确定管道沿线的H2S水平,其中很少考虑可能导致酸性条件的情况。还进行了风险评估,以确定各种情景的影响和缓解措施。根据研究,在特定的瞬态情况下,由于H2S水平超过了含硫服务限值,预计部分管道将暴露于含硫服务条件下。概述了涉及化学品注入、过程控制和保障及操作程序的具体缓解措施。该研究成功地展示了管道材料的优化选择方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Hybrid Pipeline Fit for Purpose for Multiphase Gas and Condensate Transportation
Corrosion and materials degradation factors during normal and abnormal operating conditions are among the essential criterion in evaluating materials suitability for an offshore pipeline transporting treated gas and condensate with contaminants i.e. CO2, Materials resistant to wet H2S damage in accordance with ISO 15156 requirements and mercury. A thorough study was conducted to ascertain the pipeline section that will be exposed to sour service conditions due to substantial Materials resistant to wet H2S damage in accordance with ISO 15156 requirements level along the pipeline during certain transient scenarios. The study was conducted in view of fit-for-purpose solution and CAPEX optimization initiatives for the project. During certain transient scenarios, there is potential exposure to substantial H2S level under wet conditions for a certain pipeline length which increases materials susceptibility to wet H2S damage such as Hydrogen Induced Cracking (HIC)/Stepwise Cracking (SWC) and Sulfide Stress Cracking (SSC). Flow assurance modeling with compositional tracking module was used to determine the level of H2S along the pipeline where few potential scenarios leading to sour conditions were considered. Risk assessments were also conducted to ascertain the impact and mitigations for the scenarios. Based on studies, exposure to sour service conditions is expected at a partial length of the pipeline as the H2S level exceeds the sour service limit during specific transient scenarios. Specific mitigation measures involving chemical injection, process control and safeguarding and operating procedures were outlined. The study successfully demonstrated an optimized materials selection approach for the pipeline.
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