{"title":"Characterization of the pressure, temperature, and phase evolution during pipeline leakage in full-size ethane high-pressure gas pipeline","authors":"Jianbo Ma, Zihao Xiu, Zhenyi Liu, Mingzhi Li, Pengliang Li, Shuhong Li, Ranran Li","doi":"10.1016/j.csite.2025.106020","DOIUrl":null,"url":null,"abstract":"<div><div>A leak may occur in the ethane transport pipeline during operation, which brings serious pipeline transportation risks. Exploring the pressure, temperature and phase evolution during pipeline leakage is the basis for constructing pipeline safety technology. To this end, a full-scale ethane pipeline experimental platform was established to carry out leakage experiments at different diameters, and the pressure, temperature, and phase changes of the ethane inside the pipeline and the temperature changes of the pipeline outer wall were investigated. The experimental results show that during the ethane injection process, the turning point of the pressure increase rate is 4.26 MPa; the turning point of the temperature decrease rate is 14.26 °C and 12.07 °C. During the overall process of leakage, the ethane temperature showed the trend of \"near hot and far cold\" from the leakage port position. The critical diameter for the maximum temperature-difference and phase change time difference between the near and far ends of the leakage port is 15 mm, and the temperature-difference reaches 5.49 °C, the time difference of 121 s, which show a tendency of increasing and then decreasing when leakage diameter increase. In addition, the temperature of the outer wall of the pipeline shows the trend of \"near cold and far hot\" from the leakage port position, and the temperature of the center point of the pipeline is higher. The temperature-trough difference between different monitoring points shows a tendency to increase with the increase of leakage diameter, reaching a maximum of 5.81 °C. The conclusion of the study provides guidance for the investigation of the changing characteristics including temperature, pressure and phase state in the process of ethane pipeline leakage, which is helpful for the construction of pipeline safety technology system.</div></div>","PeriodicalId":9658,"journal":{"name":"Case Studies in Thermal Engineering","volume":"69 ","pages":"Article 106020"},"PeriodicalIF":6.4000,"publicationDate":"2025-03-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Case Studies in Thermal Engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2214157X25002801","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"THERMODYNAMICS","Score":null,"Total":0}
引用次数: 0
Abstract
A leak may occur in the ethane transport pipeline during operation, which brings serious pipeline transportation risks. Exploring the pressure, temperature and phase evolution during pipeline leakage is the basis for constructing pipeline safety technology. To this end, a full-scale ethane pipeline experimental platform was established to carry out leakage experiments at different diameters, and the pressure, temperature, and phase changes of the ethane inside the pipeline and the temperature changes of the pipeline outer wall were investigated. The experimental results show that during the ethane injection process, the turning point of the pressure increase rate is 4.26 MPa; the turning point of the temperature decrease rate is 14.26 °C and 12.07 °C. During the overall process of leakage, the ethane temperature showed the trend of "near hot and far cold" from the leakage port position. The critical diameter for the maximum temperature-difference and phase change time difference between the near and far ends of the leakage port is 15 mm, and the temperature-difference reaches 5.49 °C, the time difference of 121 s, which show a tendency of increasing and then decreasing when leakage diameter increase. In addition, the temperature of the outer wall of the pipeline shows the trend of "near cold and far hot" from the leakage port position, and the temperature of the center point of the pipeline is higher. The temperature-trough difference between different monitoring points shows a tendency to increase with the increase of leakage diameter, reaching a maximum of 5.81 °C. The conclusion of the study provides guidance for the investigation of the changing characteristics including temperature, pressure and phase state in the process of ethane pipeline leakage, which is helpful for the construction of pipeline safety technology system.
期刊介绍:
Case Studies in Thermal Engineering provides a forum for the rapid publication of short, structured Case Studies in Thermal Engineering and related Short Communications. It provides an essential compendium of case studies for researchers and practitioners in the field of thermal engineering and others who are interested in aspects of thermal engineering cases that could affect other engineering processes. The journal not only publishes new and novel case studies, but also provides a forum for the publication of high quality descriptions of classic thermal engineering problems. The scope of the journal includes case studies of thermal engineering problems in components, devices and systems using existing experimental and numerical techniques in the areas of mechanical, aerospace, chemical, medical, thermal management for electronics, heat exchangers, regeneration, solar thermal energy, thermal storage, building energy conservation, and power generation. Case studies of thermal problems in other areas will also be considered.