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 , He Li , Hui Feng , Xiong Liu , 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 , He Li , Hui Feng , Xiong Liu , 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}
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.
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.