化工学报 ›› 2025, Vol. 76 ›› Issue (7): 3742-3751.DOI: 10.11949/0438-1157.20241507

• 过程安全 • 上一篇    

CO2管道不同相态节流放空特性研究与对比

范振宁1(), 梁海宁1, 房茂立1, 赫一凡2, 于帅2, 闫兴清2, 安佳然2, 乔帆帆2, 喻健良2()   

  1. 1.中石化石油工程设计有限公司,山东 东营 257099
    2.大连理工大学化工学院,辽宁 大连 116024
  • 收稿日期:2024-12-25 修回日期:2025-03-17 出版日期:2025-07-25 发布日期:2025-08-13
  • 通讯作者: 喻健良
  • 作者简介:范振宁(1985—),男,硕士,高级工程师,jh05-128@163.com

Research and comparison of throttling and venting characteristics of CO2 pipelines in different phase states

Zhenning FAN1(), Haining LIANG1, Maoli FANG1, Yifan HE2, Shuai YU2, Xingqing YAN2, Jiaran AN2, Fanfan QIAO2, Jianliang YU2()   

  1. 1.Sinopec Petroleum Engineering Corporation, Dongying 257099, Shandong, China
    2.School of Chemical Engineering, Dalian University of Technology, Dalian 116024, Liaoning, China
  • Received:2024-12-25 Revised:2025-03-17 Online:2025-07-25 Published:2025-08-13
  • Contact: Jianliang YU

摘要:

基于工业规模CO2管道放空实验平台,开展了密相和超临界相CO2节流放空实验。通过对放空实验的结果进行分析和对比,揭示了不同初始相态CO2放空过程中,放空管管内CO2的压力、温度和相态的演变规律和差异,为实际工业CO2管道放空操作提供直接的数据支持和参考建议。结果表明,密相和超临界相CO2放空过程阀门上游截面和下游截面压力会分别经历快速降压阶段和充压阶段。各截面温度演变过程均会经历两段温降和温升过程。相较密相CO2放空,超临界相CO2放空阀门前后截面的压差更大,这可能会对阀门造成更为强烈的冲击。然而,尽管可能存在上述问题,超临界相CO2放空相较密相CO2放空管内CO2可以更早脱离气液饱和相。因此,超临界CO2放空时管内发生干冰冻堵的风险也相对较低。

关键词: 安全, 二氧化碳, 实验验证, CO2管道, 放空特性, CO2相态

Abstract:

Based on an industrial-scale CO2 pipeline venting experimental platform, throttling and venting experiments were conducted for both dense-phase and supercritical CO2. Through the analysis and comparison of the experimental results, this study reveals the evolution patterns and differences in pressure, temperature, and phase state of CO2 within the venting pipeline during the release process under different initial phase conditions. The findings provide direct data support, valuable insights, and practical recommendations for CO2 pipeline venting operations in industrial applications. The results show that during both subcritical and supercritical CO2 venting, the pressure at the upstream and downstream sections of the valve undergoes distinct phases: a rapid depressurization stage followed by a pressurization stage at the upstream and downstream sections, respectively. The downstream pressure then decreases as the main pipeline pressure drops. The temperature evolution at each section follows a two-stage process of cooling and heating, corresponding to the initial valve opening and the subsequent throttling phase. After the valve is fully opened, the temperature drop is more pronounced during dense-phase CO2 venting, with the minimum temperatures inside the pipeline being -35.75℃ for dense-phase CO2 and -28.63℃ for supercritical CO2. This indicates that dense-phase CO2 undergoes a greater temperature drop during venting. Furthermore, the pressure differential across the valve is greater during supercritical CO2 venting than during dense-phase CO2 venting, which could result in more significant valve shock. However, despite the above problems, the CO2 in the supercritical CO2 venting pipe can leave the gas-liquid saturation phase earlier than that in the dense-phase CO2 venting pipe. Overall, the study provides valuable insights into the behavior of CO2 under different phases during venting and offers practical guidance for optimizing CO2 pipeline venting operations to enhance safety, performance, and operational efficiency.

Key words: safety, carbon dioxide, experimental verification, CO2 pipeline, venting characteristics, CO2 phase state

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