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    • 2. 发明申请
    • METHOD AND APPARATUS FOR LIQUEFYING A HYDROCARBON STREAM
    • 用于液化石油气流的方法和装置
    • WO2008006867A2
    • 2008-01-17
    • PCT/EP2007/057134
    • 2007-07-12
    • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.JAGER, Marco DickKAART, Sander
    • JAGER, Marco DickKAART, Sander
    • F25J1/0292F25J1/0022F25J1/0055F25J1/0057F25J1/0212F25J1/0214F25J1/0215F25J1/0216F25J1/0254F25J1/0268F25J1/0291F25J2245/02
    • A method of liquefying a hydrocarbon stream such as natural gas from a feed stream (10) comprising at least the steps of: (a) passing the feed stream (10) against a mixed refrigerant being cycled through a heat exchanger (12), to provide an at least partly liquefied hydrocarbon stream (20) having a temperature below -100 °C; (b) outflowing the mixed refrigerant as a liquid and vapour outflow refrigerant stream (80) from the heat exchanger (12); (c) passing the liquid and vapour outflow refrigerant stream (80) through a first separator (18) to provide a vapour refrigerant stream (90) and a liquid refrigerant stream (110); (d) recycling without substantial heat exchange the liquid refrigerant stream (110) of step (c) into the heat exchanger (12) of step (a); (e) compressing the vapour refrigerant stream (90) to provide a compressed refrigerant stream (95); (f) cooling the compressed refrigerant stream (95) to provide a cooled compressed stream (100) having a temperature below 0 °C; and (g) recycling the cooled compressed stream (100) into the heat exchanger (12) of step (a).
    • 一种从进料流(10)液化烃流如天然气的方法,包括至少以下步骤:(a)将进料流(10)通过循环通过热交换器(12)的混合制冷剂通入到 提供温度低于-100℃的至少部分液化的烃流(20); (b)从所述热交换器(12)将混合制冷剂作为液体和蒸汽流出制冷剂流(80)流出; (c)使液体和蒸气流出的制冷剂流(80)通过第一分离器(18),以提供蒸气制冷剂流(90)和液体制冷剂流(110); (d)将步骤(c)的液体制冷剂流(110)实质上热交换到步骤(a)的热交换器(12)中循环; (e)压缩蒸汽制冷剂流(90)以提供压缩的制冷剂流(95); (f)冷却压缩的制冷剂流(95)以提供温度低于0℃的冷却的压缩流(100); 和(g)将冷却的压缩物流(100)再循环到步骤(a)的热交换器(12)中。
    • 4. 发明申请
    • REFRIGERANT CIRCUIT
    • 制冷电路
    • WO2007068730A1
    • 2007-06-21
    • PCT/EP2006/069693
    • 2006-12-14
    • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.KAART, SanderKLEIN NAGELVOORT, Robert
    • KAART, SanderKLEIN NAGELVOORT, Robert
    • F25J1/02F25B1/10
    • F25B1/10F25B2400/075F25B2400/13F25J1/0022F25J1/0052F25J1/0294
    • The present invention relates to a refrigerant circuit (1), in particular for use in a liquefaction plant, the refrigerant circuit (1) at least comprising: - a refrigerator (2) having an inlet (21) for refrigerant (10) at a refrigeration pressure, and at least five outlets (22, 23, 24, 25, 26, ...) for evaporated refrigerant (20, 30, 40, 50, 60, ...) evaporated at different pressure levels, the at least five outlets (22, 23, 24, 25, 26, ...) being preferably intended for refrigerants evaporated at increasing pressures from the first outlet (22) to the fifth (26) and optional higher outlets; - a first compressor (3) having one or more inlets for receiving evaporated refrigerant from the refrigerator and an outlet (34) that can be connected to the inlet (21) of the refrigerator (2); and - a second compressor (4) having one or more inlets for receiving evaporated refrigerant from the refrigerator and an outlet (44) that can be connected to the inlet (21) of the refrigerator (2).
    • 本发明涉及一种特别用于液化装置的制冷剂回路(1),所述制冷剂回路(1)至少包括: - 一冷藏库(2),具有用于制冷剂(10)的入口(21) 制冷压力和至少五个用于蒸发的制冷剂(20,30,40,50,60,...)的出口(22,23,24,25,26 ...)在不同压力水平下蒸发,至少 五个出口(22,23,24,25,26,...)优选地用于在从第一出口(22)到第五(26)和任选的更高出口的增加的压力下蒸发的制冷剂; - 具有一个或多个入口的第一压缩机(3),用于从冰箱接收蒸发的制冷剂和可连接到冰箱(2)的入口(21)的出口(34); 以及 - 第二压缩机(4),其具有一个或多个用于从冷藏库接收蒸发的制冷剂的入口和可连接到冰箱(2)的入口(21)的出口(44)。
    • 9. 发明申请
    • METHODS AND APPARATUSES FOR COOLING AND/OR LIQUEFYING A HYDROCARBON STREAM
    • 用于冷却和/或液化石油气流的方法和装置
    • WO2009050178A2
    • 2009-04-23
    • PCT/EP2008/063833
    • 2008-10-15
    • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.KAART, Sander
    • KAART, Sander
    • F25J1/02F25B1/053F25B49/02F04D27/02
    • F25J1/0298F25B41/00F25B2400/13F25B2400/16F25B2400/23F25J1/0022F25J1/0052F25J1/0087F25J1/0249F25J1/0279F25J1/0283F25J1/0294
    • A hydrocarbon stream (5) is heat exchanged against one or more at least partially condensed refrigerant streams (2Oe) to provide a cooled hydrocarbon stream (6) and an at least partly evaporated refrigerant stream (8) at a pressure Pl. One or more compressor feed streams (10a) are provided at a pressure not higher than Pl, from a combination of at least at least a fraction of the at least partly evaporated refrigerant stream (8) and an at least partially liquid stream (32) which is at least partly vapourised to cool at least one of the one or more compressor feed streams (10a). The at least partially liquid stream (32) is provided from the at least one refrigerant circuit (2). At least one of the refrigerant compressor ( s ) is operated, thereby providing at least one or more compressed refrigerant streams (20), of which at least a portion is condensed to provide the one or more at least partly condensed refrigerant streams (2Oe). Optionally, a vapour recirculation line (12) may be provided and brought in a vapour recirculation mode, whereby the one or more compressor feed streams (10a) is made to comprise a vapour recirculation stream (30) consisting of a vaporous portion of the at least one of the one or more compressed refrigerant streams (20).
    • 烃流(5)与一个或多个至少部分冷凝的制冷剂流(20e)进行热交换,以在压力P1下提供冷却的烃流(6)和至少部分蒸发的制冷剂流(8)。 至少部分蒸发的制冷剂流(8)的至少一部分和至少部分蒸发的制冷剂流(8)的组合与至少部分液体流(32)的组合,在不高于P1的压力下提供一个或多个压缩机进料流(10a) 其至少部分蒸发以冷却所述一个或多个压缩机进料流(10a)中的至少一个。 所述至少部分液体流(32)由所述至少一个制冷剂回路(2)提供。 至少一个制冷剂压缩机被操作,从而提供至少一个或多个压缩的制冷剂流(20),其中至少一部分被冷凝以提供一个或多个至少部分冷凝的制冷剂流(20e) 。 可选地,可以提供蒸汽再循环管线(12)并使其进入蒸气再循环模式,由此一个或多个压缩机进料流(10a)被制成包括由蒸气再循环流(30) 一个或多个压缩制冷剂流(20)中的至少一个。