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METHOD FOR PRODUCING A UNITED GAS-HYDROCARBON FLOW AND LIQUID HYDROCARBON FLOWS AND DEVICE FOR ITS IMPLEMENTATION

机译:产生气-烃流和液化烃流的方法及其实施装置

摘要

1. A method of obtaining a combined gaseous hydrocarbon stream (260) and liquid hydrocarbon streams (90, 100) from at least two multiphase hydrocarbon streams (10, 20), which includes at least the stages: (1) using the first a production line (A) comprising a first pipeline (10) for a first multiphase hydrocarbon stream (10) from one or more first hydrocarbon wells (30), a first receiving separator (50) that separates the first multiphase hydrocarbon stream (10) to obtain first gaseous a hydrocarbon stream (70) and a first liquid hydrocarbon stream (90), and a first low pressure separator (110) that separates the first liquid hydrocarbon stream (90) to obtain a first feed condensate stream (130) and a first head gaseous hydrocarbon stream (150) ); (2) using a second production line (B) containing a second pipeline (20) for a second multiphase hydrocarbon stream (30) from one or more second hydrocarbon wells (40), a second receiving separator (60) that separates the second multiphase carbohydrate a hydrogen stream (20) to obtain a second gaseous hydrocarbon stream (80) and a second liquid hydrocarbon stream (100), and a second low pressure separator (120) that separates the second liquid hydrocarbon stream (100) to obtain a second feed condensate stream ( 140) and a second head gaseous hydrocarbon stream (160); and (3) combining a second gaseous hydrocarbon stream (80), downstream from the second production line (B), with the first gaseous hydrocarbon stream (70), downstream from the first process�
机译:1.一种从至少两个多相烃物流(10、20)获得气态烃物流(260)和液态烃物流(90、100)的组合的方法,该方法至少包括以下步骤:(1)使用第一阶段生产线(A),其包括用于从一个或多个第一烃井(30)流出的第一多相烃物流(10)的第一管线(10),将第一多相烃物流(10)分离为第一组分的第一接收分离器(50)。获得第一气态烃物流(70)和第一液态烃物流(90),以及将第一液态烃物流(90)分离以获得第一进料冷凝物流(130)的第一低压分离器(110)。第一塔顶气态烃物流(150)); (2)使用第二生产线(B),第二生产线(B)包含用于从一个或多个第二烃井(40)流出的第二多相烃物流(30)的第二管道(20),分离第二多相的第二接收分离器(60)碳水化合物,氢气流(20)获得第二气态烃流(80)和第二液态烃流(100),以及第二低压分离器(120),该低压分离器将第二液态烃流(100)分离以获得第二气态烃流进料冷凝物流(140)和第二塔顶气态烃物流(160); (3)将第二生产线(B)下游的第二气态烃物流(80)与第一工艺下游的第一气态烃物流(70)合并。

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