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液氨卧罐液体实时连续泄漏建模及分析

  • 何娟霞 ,
  • 周冬梅 ,
  • 刘磊 ,
  • 周琪勇 ,
  • 黄丽文 ,
  • 姚健庭
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  • 1. 广西大学资源环境与材料学院,广西 南宁 530004 2. 华南理工大学材料科学与工程学院,广东 广州 510641

收稿日期: 2020-06-04

  修回日期: 2020-07-04

  网络出版日期: 2021-06-28

基金资助

2016年度广西科技厅重点研发计划

Modeling and analysis of liquid real-time continuous leakage in horizontal liquid ammonia tank

  • HE Juan-Xia ,
  • ZHOU Dong-Mei ,
  • LIU Lei ,
  • ZHOU Qi-Yong ,
  • HUANG Li-Wen ,
  • YAO Jian-Ting
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  • 1. College of Resources, Environment and Materials, Guangxi University, Nanning, Guangxi 530004, China 2. College of Materials Science and Engineering, South China University of Technology, Guangzhou, Guangdong 510641, China

Received date: 2020-06-04

  Revised date: 2020-07-04

  Online published: 2021-06-28

摘要

基于范德瓦耳斯方程和流体力学理论,考虑液氨卧罐泄漏时罐压和液面面积变化,建立了液氨卧罐液体实时连续泄漏模型。利用模型对某制冷企业液氨卧罐进行数学模拟,并将计算结果与PHAST模拟结果进行对比分析。结果表明,液面高度h下降幅度先减缓后变大,液体泄漏质量流率Qm和泄漏孔处液体泄漏速率v的下降幅度及泄漏液体质量m的增加幅度逐渐减缓。泄漏开始时,Qm和v值最大;泄漏停止时,m值最大。泄漏孔径为5, 30和100 mm时,泄漏时间t为29884.027, 837.289和77.550 s,Qm(max)为0.552, 19.913和221.160 kg/s,v(max)为46.733 m/s,m(max)为10255.649, 10339.923和10572.760 kg。模型计算结果与PHAST模拟结果偏差小于24%,从参数变化规律和风险应急分析,模型对液氨卧罐液体泄漏理论计算具有一定适用性。

本文引用格式

何娟霞 , 周冬梅 , 刘磊 , 周琪勇 , 黄丽文 , 姚健庭 . 液氨卧罐液体实时连续泄漏建模及分析[J]. 过程工程学报, 2021 , 21(6) : 731 -740 . DOI: 10.12034/j.issn.1009-606X.220171

Abstract

Based on Van der Waals equation and theory of fluid mechanics, the liquid real-time continuous leakage model of horizontal liquid ammonia tank was established considering the changes of tank pressure and liquid surface area. Mathematical modeling of a horizontal liquid ammonia tank in a refrigeration company was performed by this model, and the calculation results were compared with PHAST simulation results. The results showed that the decreasing range of liquid level height h grew slowly and then increased quickly, the decreasing range of liquid leakage mass flow rate Qm and liquid leakage rate v and the increasing range of liquid leakage mass m decrease slowly. At the beginning of leakage, Qm and v were the maximum values, at the end of leakage, m was the maximum values. When the diameters of leakage hole were 5, 30 and 100 mm, leakage time t were 29884.027, 837.289, 77.550 s, Qm(max) were 0.552, 19.913 and 221.160 kg/s, v (max) was 46.733 m/s, m(max) were 10255.649, 10339.923 and 10572.760 kg, respectively. The deviation between the calculation results of the model and the PHAST simulation results was less than 24%. From the analysis of parameter variation and risk emergency, the model had the certain applicability for the theoretical calculation of liquid leakage in horizontal liquid ammonia tank.
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