首页|段塞工况下三相分离器的设计

段塞工况下三相分离器的设计

扫码查看
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.
Design of three-phase separator under slug condition
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.

three-phase separationdesignsimulationslugoil-gas-water three-phase flow

关艳玲、付丽君、张亮、关艳艳、卫兵

展开 >

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

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

三相分离 设计 模拟 段塞 油气水三相流

国网黑龙江省电力有限公司科技项目

52243723000W

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
年,卷(期):2024.45(4)
  • 19