主管:中华人民共和国应急管理部
主办:应急管理部天津消防研究所
ISSN 1009-0029  CN 12-1311/TU

消防科学与技术 ›› 2026, Vol. 45 ›› Issue (4): 104-109.

• • 上一篇    下一篇

基于LPG组分特性的二相泄漏模型研究

俞依澜1,2, 苏隆隆1,2, 付雨霏1,2, 李龙硕1,2, 葛巍巍1,2   

  1. (1.中国消防救援学院,北京 102202; 2.工业与公共建筑火灾防控技术应急管理部重点实验室,北京 102202)
  • 收稿日期:2025-01-02 修回日期:2025-02-08 出版日期:2026-04-15 发布日期:2026-04-15
  • 作者简介:俞依澜,中国消防救援学院消防工程专业,主要从事危化品救援、防排烟工程研究,北京市昌平区南雁路4号,102202。
  • 基金资助:
    国家重点研发计划(2023YFC3011205)

Construction of a two-phase leakage model based on the properties of LPG components

Yu Yilan1,2, Su Longlong1,2, Fu Yufei1,2, Li Longshuo1,2, Ge Weiwei1,2   

  1. (1. China Fire and Rescue Institute, Beijing 102202, China; 2. Laboratory of Fire Protection Technology for Industry and Public Building, Ministry of Emergency Management, Beijing 102202, China)
  • Received:2025-01-02 Revised:2025-02-08 Online:2026-04-15 Published:2026-04-15

摘要: 根据LPG中主要组分的理化性质,利用Aspen Plus软件绘制丙烷-丁烷二元体系的液汽平衡相图,分析发现,LPG泄漏后,液相中的丙烷会立即闪蒸汽化,而丁烷会形成液池再蒸发汽化,据此分别建立丙烷和丁烷两个泄漏模型。在计算分子间作用力、扩散系数、混合气体爆炸极限等关键问题参数后,按照多源气体泄漏数值模拟的方法构建了LPG的二相泄漏模型。通过对一起LPG罐车泄漏事故模拟发现,丙烷、丁烷在扩散过程中会呈现截然不同的气体浓度分布,影响整个危险区域范围,因此在对LPG泄漏事故模拟时不能忽略组分因素的影响。通过与Burro 8号试验数据对比,验证了构建的二相泄漏模型能较好地反映LPG泄漏事故真实情况。

关键词: LPG储罐, 液气平衡相图, 爆炸极限, 高斯扩散模型

Abstract: This study uses Aspen Plus software to draw the vapor-liquid equilibrium phase diagram of the propan-butane binary system based on the physicochemical properties of propane and butane. Through analysis, it was found that after LPG leakage, propane in the liquid phase will immediately vaporize, while butane will form a liquid pool and then evaporate and vaporize. Based on these findings, two distinct leakage models for propane and butane were developed respectively. Subsequently, after calculating key parameters such as intermolecular forces, diffusion coefficients, and explosion limits of mixed gases, a two-phase LPG leakage model was established through multi-source gas leakage numerical simulation method. Through the simulation of a LPG tanker leak accident, it was found that propane and butane exhibit completely different gas concentration distributions during the diffusion process, which affects the entire hazardous area. Therefore, the influence of component factors cannot be ignored when simulating LPG leak accidents. Comparative analysis with the Burro 8 experimental dataset demonstrates favorable agreement, validating the model's capability to accurately replicate real-world LPG leakage scenarios.

Key words: LPG storage tank, vapor-liquid equilibrium phase diagram, explosion limit, Gaussian dispersion model