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    • 2. 发明申请
    • METHOD AND APPARATUS FOR TREATING A HYDROCARBON STREAM
    • 处理油气田的方法和装置
    • US20100162753A1
    • 2010-07-01
    • US12438032
    • 2007-08-21
    • Eduard Coenraad BrasJill Hui Chiun ChiengAkash Damodar Wani
    • Eduard Coenraad BrasJill Hui Chiun ChiengAkash Damodar Wani
    • F25J1/00
    • F25J3/0209F25J3/0214F25J3/0233F25J3/0238F25J2200/02F25J2205/04F25J2205/30F25J2210/62F25J2240/02F25J2270/904
    • The present invention relates to a method of treating a hydrocarbon stream, the method at least comprising the steps of: supplying a partly condensed feed stream (10). to a first gas/liquid separator (2) and into a gaseous stream (2 and a liquid stream (30); expanding the liquid stream (30) and the gaseous stream (20) and subsequently feeding them into a second gas/liquid separator (3) at a first and second feeding point (32) respectively, the second feeding point (32) being at a higher level than the first feeding point (31); feeding a liquefied natural gas stream (70,70b) into the second gas/liquid separator (3) at a third feeding point (33) being at a higher level than the second feeding point (32); removing from the top of the second gas/liquid separator (3) a C2+ lean gaseous stream (60) and from the bottom a liquid stream (80, 80a); wherein the liquefied ̂natural gas stream (70,70b) is obtained from a source (4) of liquefied natural gas from a separate plant.
    • 本发明涉及一种处理烃流的方法,所述方法至少包括以下步骤:供应部分冷凝的进料流(10)。 到第一气/液分离器(2)并进入气流(2和液体流);使液体流(30)和气流(20)膨胀,然后将它们送入第二气/液分离器 (3)分别在第一和第二进料点(32)处,所述第二进料点(32)处于比所述第一进料点(31)更高的水平;将液化的天然气流(70,70b)进料到所述第二进料点 在第三进料点(33)处的气/液分离器(3)处于比第二进料点(32)更高的水平;从第二气/液分离器(3)的顶部除去C2 +贫气流 )和从底部流出液体流(80,80a);其中液化天然气流(70,70b)从来自独立设备的液化天然气源(4)获得。
    • 4. 发明申请
    • METHOD AND APPARATUS FOR TREATING A HYDROCARBON STREAM
    • 处理油气田的方法和装置
    • US20100064725A1
    • 2010-03-18
    • US12446622
    • 2007-10-23
    • Jill Hui Chiun ChiengAkash Damodar Wani
    • Jill Hui Chiun ChiengAkash Damodar Wani
    • F25J3/00B01D53/18B01D19/00
    • F25J3/0209F25J3/0233F25J3/0238F25J2200/02F25J2200/70F25J2205/04F25J2210/62F25J2240/02F25J2270/904F25J2290/12
    • In a method of treating a hydrocarbon stream, such as a natural gas stream, a partly condensed feed stream (10) is supplied to a first gas/liquid separator (2), where it is separated into a gaseous stream (20) and a liquid stream (30). The liquid stream (30) is expanded and fed (40) into a second gas/liquid separator (3), and the gaseous stream (20) is split into at least two sub-streams (50, 70). A first sub-stream (50) of the at least two sub-streams is expanded, thereby obtaining an at least partially condensed first sub-stream (60), and subsequently fed (60) into the second gas/liquid separator (3). A second sub-stream (70) of the at least two sub-streams is cooled against a cold stream (120), thereby obtaining an at least partially condensed second sub-stream (90, 90a), which is fed (90, 90a) into the second gas/liquid separator (3) from which a gaseous stream (130) and a liquid stream (100, 100a) are removed. The at least partially condensed second sub-stream (90, 90a) may have a temperature of below −95° C.
    • 在处理烃流(例如天然气流)的方法中,将部分冷凝的进料流(10)供应到第一气/液分离器(2),在其中将其分离成气流(20)和 液体流(30)。 液体流(30)膨胀并进料(40)到第二气/液分离器(3)中,气流(20)被分成至少两个子流(50,70)。 使至少两个子流的第一子流(50)膨胀,从而获得至少部分冷凝的第一子流(60),并随后将其进料(60)进入第二气/液分离器(3) 。 所述至少两个子流的第二子流(70)针对冷流(120)冷却,从而获得至少部分冷凝的第二子流(90,90a),其被馈送(90,90a) )到第二气/液分离器(3)中,从中除去气流(130)和液流(100,100a)。 至少部分冷凝的第二子流(90,90a)可具有低于-95℃的温度。