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    • 4. 发明申请
    • METHOD AND APPARATUS FOR COOLING AND/OR LIQUEFYING A HYDROCARBON STREAM
    • 用于冷却和/或液化烃流的方法和装置
    • WO2009071538A3
    • 2010-03-11
    • PCT/EP2008066623
    • 2008-12-02
    • SHELL INT RESEARCHCHANTANT FRANCOISPOH CHUN KIT
    • CHANTANT FRANCOISPOH CHUN KIT
    • F25J1/02F25B1/10
    • F25J1/0052F25B1/10F25B5/04F25B2400/13F25J1/0022F25J1/0087F25J1/0294
    • A refrigerant stream (10) is provided at a refrigerant pressure, and passed through at least three heat exchange steps (12, 14, 16, 18) operating at different pressure levels. A hydrocarbon stream (20) is passed through at least two of these heat exchange steps to provide a cooled hydrocarbon stream (30). A fraction of the refrigerant stream (10) is expanded and evaporated at each heat exchange step (12, 14, 16, 18) to a different pressure, to provide a first evaporated refrigerant stream (40) at a first evaporation pressure, and at least two other evaporated refrigerant streams (50, 60, 70) at evaporation pressures lower than the first evaporation pressure. The first evaporated refrigerant stream (40) is compressed through a highest-pressure compressor stage (22) to provide at least a fraction of the refrigerant stream (10) at the refrigerant pressure, and the other evaporated refrigerant streams (50, 60, 70) are compressed through at least two parallel lower pressure compressor stages (24, 26, 28) to provide two or more part-compressed refrigerant streams (50a, 60a, 70a), all of which part-compressed refrigerant streams (50a, 60a, 70a) being passed through the highest pressure compressor stage (22).
    • 制冷剂流(10)以制冷剂压力提供,并且通过在不同压力水平下操作的至少三个热交换步骤(12,14,16,18)。 烃流(20)通过这些热交换步骤中的至少两个以提供冷却的烃流(30)。 一部分制冷剂流(10)在每个热交换步骤(12,14,16,18)处被膨胀和蒸发到不同的压力,以在第一蒸发压力下提供第一蒸发的制冷剂流(40) 至少两个蒸发的制冷剂流(50,60,70),其蒸发压力低于第一蒸发压力。 第一蒸发的制冷剂流(40)通过最高压力的压缩机级(22)被压缩,以在制冷剂压力下提供至少一部分制冷剂流(10),另一个蒸发的制冷剂流(50,60,70 )通过至少两个平行的低压压缩机级(24,26,28)压缩,以提供两个或更多个部分压缩的制冷剂流(50a,60a,70a),所有这些部分压缩的制冷剂流(50a,60a,70a) 70a)通过最高压力的压缩机级(22)。
    • 9. 发明申请
    • METHOD OF TREATING A HYDROCARBON STREAM COMPRISING METHANE, AND AN APPARATUS THEREFOR
    • 处理包含甲烷的烃流的方法及其装置
    • WO2012000998A2
    • 2012-01-05
    • PCT/EP2011060826
    • 2011-06-28
    • SHELL INT RESEARCHBUIJS CORNELISCHANTANT FRANCOIS
    • BUIJS CORNELISCHANTANT FRANCOIS
    • F25J1/02C10L3/10
    • B01D53/0462C10L3/106F25J1/0022F25J1/0052F25J1/0055F25J1/0212F25J1/0214F25J1/0238F25J2220/68F25J2290/12
    • A wet hydrocarbon stream (510) comprising at least methane and water, provided at a temperature equal to a first temperature, is cooled thereby lowering the temperature to a second temperature. In a water removal device (525) at least one wet disposal stream (590) comprising water is withdrawn from the wet hydrocarbon stream, at the second temperature. An effluent stream (560), comprising the wet hydrocarbon stream from which the at least one wet disposal stream (590) has been removed, is discharged from the water removal device (525) and passed to a further heat exchanger (535). At least one refrigerant stream (210) is also passed to the further heat exchanger (535), and both the effluent stream (560) and the refrigerant stream (210) are cooled in the further heat exchanger (535) by indirect heat exchanging against an evaporating refrigerant fraction (230). The effluent stream (560) is heated by indirectly heat exchanging against the wet hydrocarbon stream (510), wherein said cooling of the wet hydrocarbon stream (510) comprises this indirectly heat exchanging.
    • 在等于第一温度的温度下提供的至少包含甲烷和水的湿烃流(510)被冷却,从而将温度降至第二温度。 在除水装置(525)中,在第二温度下,从湿烃流中排出包含水的至少一个湿处理流(590)。 包含从其中去除了至少一个湿式处理流(590)的湿烃物流的排出物流(560)从除水装置(525)排出,并通入另一个热交换器(535)。 至少一个制冷剂流(210)也被传送到另外的热交换器(535),并且流出物流(560)和制冷剂流(210)都在另一个热交换器(535)中通过间接热交换 蒸发制冷剂馏分(230)。 通过与湿烃流(510)的间接热交换来加热流出物流(560),其中所述的冷烃流(510)的冷却包括这种间接的热交换。