能源化工2024,Vol.45Issue(4) :25-29.

段塞工况下三相分离器的设计

Design of three-phase separator under slug condition

关艳玲 付丽君 张亮 关艳艳 卫兵
能源化工2024,Vol.45Issue(4) :25-29.

段塞工况下三相分离器的设计

Design of three-phase separator under slug condition

关艳玲 1付丽君 1张亮 1关艳艳 2卫兵1
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作者信息

  • 1. 国网黑龙江省电力有限公司电力科学研究院,黑龙江哈尔滨 150030
  • 2. 国网黑龙江省电力有限公司经济技术研究院,黑龙江哈尔滨 150010
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摘要

三相分离器设计时应考虑管道内段塞流变化对设备的冲击,并且能够适应油气田的全周期开发过程.采用OLGA软件建立了某油田起伏管道油气水多相流瞬态模型,针对段塞流的影响计算了该油田三相分离器的尺寸,模拟分析了三相分离器对流动参数变化的适应程度.结果表明,根据管道出口位置压力、持液率、段塞长度变化计算得到液塞长度平均衰减率为2.67 m/s,停留时间选取 4 min,安全系数选取 1.5,三相分离器最终设计尺寸为 2 400 mm×7 200 mm,公称容积为 36 m3,数量为 2 台.三相分离器能够适应的最大气油比为40 m3/m3,最大液体输送流量为 700 m3/d,压力的变化对三相分离器运行几乎无影响.

Abstract

The impact of slug flow change on equipment should be considered in the design of three-phase separator,and it can adapt to the whole cycle development process of oil-gas field.A transient model of multiphase flow of oil-gas-water is established by using OLGA software.Considering the influence of slug flow,the size of three-phase separator is calculated and the adaptability of three-phase separator to the change of flow parameters is simulated and analyzed.The results show that the average attenuation rate of the liquid plug length is 2.67 m/s,the residence time is 4 min,and the safety factor is 1.5.The final design size of the three-phase separator is 2 400 mm×7 200 mm,the nominal volume is 36 m3,and the number is 2.The maximum atmospheric oil ratio of the three-phase separator can be adapted to is 40 m3/m3,and the maximum liquid conveying flow rate is 700 m3/d.The change of pressure has almost no influence on the operation of the three-phase separator.

关键词

三相分离/设计/模拟/段塞/油气水三相流

Key words

three-phase separation/design/simulation/slug/oil-gas-water three-phase flow

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基金项目

国网黑龙江省电力有限公司科技项目(52243723000W)

出版年

2024
能源化工
中国石化集团南京化学工业有限公司技术中心

能源化工

CSTPCD
影响因子:0.419
ISSN:2095-9834
参考文献量19
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