化工学报 ›› 2025, Vol. 76 ›› Issue (6): 2770-2780.DOI: 10.11949/0438-1157.20241372

• 过程系统工程 • 上一篇    下一篇

膜片压力对氢-空气混合气体泄爆过程的影响

蒋敏1,2(), 邵翔宇1,2(), 郑立刚1, 高建良1, 雷刚2   

  1. 1.河南理工大学安全科学与工程学院,河南 焦作 454003
    2.航天低温推进剂技术国家重点实验室,北京 100028
  • 收稿日期:2024-11-28 修回日期:2025-01-09 出版日期:2025-06-25 发布日期:2025-07-09
  • 通讯作者: 邵翔宇
  • 作者简介:蒋敏(1999—),女,硕士研究生,212201020049@home.hpu.edu.cn
  • 基金资助:
    航天低温推进剂技术国家重点实验室开放课题(SKLTSCP202210);河南省自然科学基金项目(242300420026);中国博士后科学基金项目(2023M730985);河南省高等学校重点科研项目计划(23A620001);河南省高校基本科研业务费专项(NSFRF240805);河南省高校基本科研业务费专项(NSFRF220422)

Effect of membrane pressure on the venting explosion process of premixed hydrogen-air gases

Min JIANG1,2(), Xiangyu SHAO1,2(), Ligang ZHENG1, Jianliang GAO1, Gang LEI2   

  1. 1.College of Safety Science and Engineering, Henan Polytechnic University, Jiaozuo 454003, Henan, China
    2.State Key Laboratory of Technologies in Space Cryogenic Propellants, Beijing 100028, China
  • Received:2024-11-28 Revised:2025-01-09 Online:2025-06-25 Published:2025-07-09
  • Contact: Xiangyu SHAO

摘要:

氢气因低点火能、宽燃烧范围的特点,泄漏后极易发生燃爆事故。为有效控制爆炸压力,泄压措施被广泛采用,其中膜片压力被认为是影响泄压效果的关键因素。基于短管道边界效应更加明显,选取长径比为10∶1的方管,开展膜片压力(Pv)范围为0 ~ 48 kPa的爆炸实验。结果表明,膜片压力的增加显著延长火焰传播时间,火焰传播速度呈先下降后升高的趋势;管道两端最大超压差值随Pv的增加而减小,与Pv = 15 kPa相比,28、39、48 kPa时管道两端压差从30.08 kPa减小至28.96、20.68和10.44 kPa;泄爆端压力-时间曲线呈双峰结构,第二峰值Pext低于初始峰值;火焰与压力的传播在初期会受到膜抗拉强度的阻滞,膜破后压力急剧攀升,火焰呈往返振荡现象,压力振幅随膜片压力的增加而显著提升。

关键词: 氢, 安全, 爆炸, 膜片压力, 火焰传播, 超压

Abstract:

Due to the characteristics of low ignition energy and wide combustion range, hydrogen is prone to explosion accidents after leakage. To effectively control explosion pressure, venting measures are widely utilized, with vent membrane thickness identified as a critical factor influencing venting performance. Based on the fact that the boundary effect of short pipes is more obvious, a square pipe with a length-to-diameter ratio of 10∶1 was selected to carry out explosion experiments with a diaphragm pressure (Pv) range of 0—48 kPa. The results indicate that an increase in membrane pressure significantly prolongs the flame propagation time, with the flame propagation velocity exhibiting a trend of initial decrease followed by an increase. The maximum overpressure difference between the two ends of the pipe decreases with increasing membrane pressure. Compared to 15 kPa, the pressure differences at 28, 39, and 48 kPa decrease from 30.08 kPa to 28.96, 20.68, and 10.44 kPa, respectively. The pressure-time curve at the venting end displays a double-peak structure, with the second peak pressure (Pext) being lower than the initial peak pressure. During the early stages, flame and pressure propagation are hindered by the tensile strength of the membrane. After the membrane ruptures, the pressure rises sharply, and the flame exhibits oscillatory propagation within the pipe. Additionally, the pressure amplitude increases significantly with higher membrane pressure.

Key words: hydrogen, safety, explosion, vent burst pressure, flame propagation, overpressure

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