高压二氧化碳管道故障的后果:全尺寸爆裂试验和数值模拟

IF 3.6 3区 工程技术 Q2 ENGINEERING, CHEMICAL Journal of Loss Prevention in The Process Industries Pub Date : 2024-11-13 DOI:10.1016/j.jlp.2024.105489
Jun Wang , He Li , Hui Feng , Xiong Liu , Cheng Lu
{"title":"高压二氧化碳管道故障的后果:全尺寸爆裂试验和数值模拟","authors":"Jun Wang ,&nbsp;He Li ,&nbsp;Hui Feng ,&nbsp;Xiong Liu ,&nbsp;Cheng Lu","doi":"10.1016/j.jlp.2024.105489","DOIUrl":null,"url":null,"abstract":"<div><div>Carbon Capture and Storage (CCS) is a widely acknowledged technique for mitigating global warming. High-pressure pipelines emerge as the most efficient and economical means to transport Carbon Dioxide (CO<sub>2</sub>) from source to storage sites. Given the hazardous nature of CO<sub>2</sub> and the potential for catastrophic consequences in an unplanned release, ensuring safe operation of CO<sub>2</sub> pipelines is paramount. This necessitates a comprehensive understanding of the potential consequences of CO<sub>2</sub> pipeline failures. This paper presents experimental measurements of CO<sub>2</sub> dispersion profiles following a full-scale burst test, simulating a real-world CO<sub>2</sub> pipeline failure scenario. The experimental setup comprised an 82.7 m buried pipeline test section with a diameter of 324 mm, connected at both ends to 60 m reservoirs. The rupture of the pipeline was initiated at the middle of the test section using an explosive charge. Measurements were carried out for the transient downwind CO<sub>2</sub> concentrations and temperatures following the explosive release. Computational Fluid Dynamics (CFD) models employing proposed numerical methods were used to simulate the experimental scenario. The performance of these methods was validated through comparisons with experimental measurements. The validated numerical methods were then employed to predict consequence distances for full-scale CO<sub>2</sub> pipeline failures in real-world scenarios.</div></div>","PeriodicalId":16291,"journal":{"name":"Journal of Loss Prevention in The Process Industries","volume":"92 ","pages":"Article 105489"},"PeriodicalIF":3.6000,"publicationDate":"2024-11-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Consequence of high-pressure CO2 pipeline failure: Full-scale burst test and numerical simulation\",\"authors\":\"Jun Wang ,&nbsp;He Li ,&nbsp;Hui Feng ,&nbsp;Xiong Liu ,&nbsp;Cheng Lu\",\"doi\":\"10.1016/j.jlp.2024.105489\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Carbon Capture and Storage (CCS) is a widely acknowledged technique for mitigating global warming. High-pressure pipelines emerge as the most efficient and economical means to transport Carbon Dioxide (CO<sub>2</sub>) from source to storage sites. Given the hazardous nature of CO<sub>2</sub> and the potential for catastrophic consequences in an unplanned release, ensuring safe operation of CO<sub>2</sub> pipelines is paramount. This necessitates a comprehensive understanding of the potential consequences of CO<sub>2</sub> pipeline failures. This paper presents experimental measurements of CO<sub>2</sub> dispersion profiles following a full-scale burst test, simulating a real-world CO<sub>2</sub> pipeline failure scenario. The experimental setup comprised an 82.7 m buried pipeline test section with a diameter of 324 mm, connected at both ends to 60 m reservoirs. The rupture of the pipeline was initiated at the middle of the test section using an explosive charge. Measurements were carried out for the transient downwind CO<sub>2</sub> concentrations and temperatures following the explosive release. Computational Fluid Dynamics (CFD) models employing proposed numerical methods were used to simulate the experimental scenario. The performance of these methods was validated through comparisons with experimental measurements. The validated numerical methods were then employed to predict consequence distances for full-scale CO<sub>2</sub> pipeline failures in real-world scenarios.</div></div>\",\"PeriodicalId\":16291,\"journal\":{\"name\":\"Journal of Loss Prevention in The Process Industries\",\"volume\":\"92 \",\"pages\":\"Article 105489\"},\"PeriodicalIF\":3.6000,\"publicationDate\":\"2024-11-13\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of Loss Prevention in The Process Industries\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S095042302400247X\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Loss Prevention in The Process Industries","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S095042302400247X","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0

摘要

碳捕集与封存(CCS)是一项广受认可的减缓全球变暖的技术。高压管道是将二氧化碳(CO2)从源头输送到储存地点的最高效、最经济的手段。鉴于二氧化碳的危险性以及意外泄漏可能造成的灾难性后果,确保二氧化碳管道的安全运行至关重要。这就需要全面了解二氧化碳管道故障的潜在后果。本文介绍了模拟真实世界二氧化碳管道故障情景的全尺寸爆裂试验后二氧化碳扩散剖面的实验测量结果。实验装置包括一个 82.7 米长、直径为 324 毫米的埋地管道试验段,两端与 60 米长的储气罐相连。使用炸药在试验段的中间位置引爆管道破裂。对爆炸释放后瞬时下风二氧化碳浓度和温度进行了测量。计算流体动力学 (CFD) 模型采用了建议的数值方法来模拟实验场景。通过与实验测量结果进行比较,验证了这些方法的性能。经过验证的数值方法随后被用于预测真实世界场景中全规模二氧化碳管道故障的后果距离。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
Consequence of high-pressure CO2 pipeline failure: Full-scale burst test and numerical simulation
Carbon Capture and Storage (CCS) is a widely acknowledged technique for mitigating global warming. High-pressure pipelines emerge as the most efficient and economical means to transport Carbon Dioxide (CO2) from source to storage sites. Given the hazardous nature of CO2 and the potential for catastrophic consequences in an unplanned release, ensuring safe operation of CO2 pipelines is paramount. This necessitates a comprehensive understanding of the potential consequences of CO2 pipeline failures. This paper presents experimental measurements of CO2 dispersion profiles following a full-scale burst test, simulating a real-world CO2 pipeline failure scenario. The experimental setup comprised an 82.7 m buried pipeline test section with a diameter of 324 mm, connected at both ends to 60 m reservoirs. The rupture of the pipeline was initiated at the middle of the test section using an explosive charge. Measurements were carried out for the transient downwind CO2 concentrations and temperatures following the explosive release. Computational Fluid Dynamics (CFD) models employing proposed numerical methods were used to simulate the experimental scenario. The performance of these methods was validated through comparisons with experimental measurements. The validated numerical methods were then employed to predict consequence distances for full-scale CO2 pipeline failures in real-world scenarios.
求助全文
通过发布文献求助,成功后即可免费获取论文全文。 去求助
来源期刊
CiteScore
7.20
自引率
14.30%
发文量
226
审稿时长
52 days
期刊介绍: The broad scope of the journal is process safety. Process safety is defined as the prevention and mitigation of process-related injuries and damage arising from process incidents involving fire, explosion and toxic release. Such undesired events occur in the process industries during the use, storage, manufacture, handling, and transportation of highly hazardous chemicals.
期刊最新文献
An emergency linkage system of urban gas pipeline network based on Bayesian network Investigations on different distribution systems for dusts inside the 20L-sphere Consequence of high-pressure CO2 pipeline failure: Full-scale burst test and numerical simulation Quantitative risk analysis of domino effect and natech accidents triggered by flood in liquor storage tank farms Synergistic inhibition characteristics and kinetics of hydrogen explosion by two-phase suppressant N2-KHCO3
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 联系我们:info@booksci.cn
Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。
Copyright © 2023 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1