刘玉强. 液化烃储罐泄压系统泄放量的计算方法[J]. 油气储运, 2016, 35(6): 612-616. DOI: 10.6047/j.issn.1000-8241.2016.06.008
引用本文: 刘玉强. 液化烃储罐泄压系统泄放量的计算方法[J]. 油气储运, 2016, 35(6): 612-616. DOI: 10.6047/j.issn.1000-8241.2016.06.008
LIU Yu-qiang. A new calculation method for the flow rate of depressuring systems in liquefied hydrocarbon tanks[J]. Oil & Gas Storage and Transportation, 2016, 35(6): 612-616. DOI: 10.6047/j.issn.1000-8241.2016.06.008
Citation: LIU Yu-qiang. A new calculation method for the flow rate of depressuring systems in liquefied hydrocarbon tanks[J]. Oil & Gas Storage and Transportation, 2016, 35(6): 612-616. DOI: 10.6047/j.issn.1000-8241.2016.06.008

液化烃储罐泄压系统泄放量的计算方法

A new calculation method for the flow rate of depressuring systems in liquefied hydrocarbon tanks

  • 摘要: 液化烃储罐发生泄漏、火灾事故时, 安全阀仅能将罐体压力限制在安全阀起跳压力和最大允许工作压力范围内, 无法起到主动泄压的作用, 设置泄压系统可以弥补这一不足。经计算分析发现, API 521-2014对泄压系统的通用性要求不适用于容积较大的液化烃储罐泄压系统的设计, 故提出了以火灾工况、泄放阀(BDV)定压下最大泄放量所需的泄放面积作为动态泄压模块输入面积的计算方法。以容积为2000 m3的液化烃储罐为例, 对10 h内液化烃储罐火灾泄放数据进行分析, 结果: 泄压系统的最高压力、最高温度、最大泄放量均出现在火灾开始阶段, 且随着泄放时间的延长逐渐减小; 轻组分在排放物料中所占比例逐渐减小, 重组分在排放物料中所占比例则逐渐增大。利用该方法设计的泄压系统可以对液化烃储罐形成有效保护。

     

    Abstract: When leakage or fire accidents occur to liquefied hydrocarbon tanks, the pressure-relieving valve could not relieve the pressure automatically, but only limit the tank body's working pressure between its onset pressure and maximum allowable working pressure. Depressuring systems are used to solve this problem. Through calculation analysis, the general requirements of API 521-2014 is not applicable to the design of depressuring systems in larger-capacity liquefied hydrocarbon tanks, a new calculation method was proposed to take the blowdown area required for the maximum flow rate at the set pressure of blowdown valve (BDV) in the fire case as the input area of dynamic depressuring module. The blowdown data of liquefied hydrocarbon tanks in the fire case within 10 h was analyzed with a 2 000 m3 liquefied hydrocarbon tank as an example. It is indicated that the maximum pressure, maximum temperature and maximum flow rate of depressuring systems all appear in the stage of fire start and decrease gradually as the depressuring process proceeds. Meanwhile, the proportion of light components in blowdown vapor declines gradually while that of heavy components rises gradually. It is concluded that the liquefied hydrocarbon tanks can be protected effectively by the depressuring systems which are designed based on this method.

     

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