Experimental study of liquefied gas dynamic leakage behavior from a pressurized vessel

被引:24
作者
Guo, Xiyan [1 ]
Tan, Wei [1 ]
Liu, Liyan [1 ]
Liu, Cenfan [2 ]
Zhu, Guorui [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] CSEI, Key Lab Special Equipment Safety & Energy Saving, Beijing 100029, Peoples R China
关键词
Small scale release experiment; Flashing jet; Two-phase flow; Model validation; R134a; LNG; RELEASE; SIMULATION; PREDICTION; EXPLOSION; SPRAY; FLOW; LPG;
D O I
10.1016/j.psep.2021.05.005
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The accidental releases of pressurized liquefied gases from tanks involve violent phase transformation, which would generate two-phase releases and flashing jets. To investigate the evolution of leakage behaviors and make an analysis of near-field jet flow characteristics, a small-scale liquefied gas release experiment has been established. Leakage holes with different length-diameter ratio (LDR) have been used to analyze interactions between the leakage holes and release behaviors. Morphological characteristics of jet expansion angles have been obtained by high-speed camera, and jet velocities have been measured by particle image velocimetry (PIV). Meanwhile, the depressurization process, variation of temperature in the tank and mass outflow rates were obtained. Results show that, despite the LDR is varying, expansion angles and jet velocities behavior in the same tendency: decreases in the initial and maintains in a stable value for a period. The stable velocity status was worked by the balanced pressure drop. Thereafter, an empirical two-phase mass outflow rate model is developed based on the experimental data, which is related to the nozzle geometric parameter and upstream pressure, 90 % of the experimental data are within +/- 12 % of the prediction. Therefore, the empirical two-phase model can be supported in the mass flow rate evaluation, especially for the release cases that LDR are smaller than 5.00 but larger than 2.00. The experimental data is beneficial for providing further insight into the prediction of accidental release and risk assessment for the liquefied gas transportation and storage. (c) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:20 / 27
页数:8
相关论文
共 35 条
[1]  
American Petroleum Institute, 2000, RISK BAS INSP BAS RE, P581
[2]   CFD analysis of the influence of a perimeter wall on the natural gas dispersion from an LNG pool [J].
Bellegoni, Marco ;
Ovidi, Federica ;
Landucci, Gabriele ;
Tognotti, Leonardo ;
Galletti, Chiara .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2021, 148 :751-764
[3]   Toxic industrial chemical (TIC) source emissions modeling for pressurized liquefied gases [J].
Britter, Rex ;
Weil, Jeffrey ;
Leung, Joseph ;
Hanna, Steven .
ATMOSPHERIC ENVIRONMENT, 2011, 45 (01) :1-25
[4]   Analysis of temperature and pressure changes in liquefied natural gas (LNG) cryogenic tanks [J].
Chen, QS ;
Wegrzyn, J ;
Prasad, V .
CRYOGENICS, 2004, 44 (10) :701-709
[5]  
[陈听宽 Chen Tingkuan], 2002, [工程热物理学报, Journal of Engineering Thermophysics], V23, P623
[6]   Quantitative risk analysis of fire and explosion on the top-side LNG-liquefaction process of LNG-FPSO [J].
Dan, Seungkyu ;
Lee, Chang Jun ;
Park, Jeongpil ;
Shin, Dongil ;
Yoon, En Sup .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2014, 92 (05) :430-441
[7]  
Daniel A.C., 1990, CHEM PROCESS SAFETY, P109
[8]   Modelling of catastrophic flashing releases [J].
Deaves, DM ;
Gilham, S ;
Mitchell, BH ;
Woodburn, P ;
Shepherd, AM .
JOURNAL OF HAZARDOUS MATERIALS, 2001, 88 (01) :1-32
[9]   Studies of injection of jet fuel at supercritical conditions [J].
Doungthip, T ;
Ervin, JS ;
Williams, TF ;
Bento, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (23) :5856-5866
[10]   Experimental study of supercritical CO2 leakage behavior from pressurized vessels [J].
Fan, Xing ;
Wang, Yangle ;
Zhou, Yuan ;
Chen, Jingtan ;
Huang, Yanping ;
Wang, Junfeng .
ENERGY, 2018, 150 :342-350