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公开(公告)号:NO323134B1
公开(公告)日:2007-01-08
申请号:NO20021896
申请日:2002-04-22
Applicant: STATOIL ASA , LINDE AG
Inventor: PAUROLA PENTTI , STOCKMANN RUDOLF , BOLT MANFRED , SAPPER RAINER
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公开(公告)号:NO20061751L
公开(公告)日:2006-06-22
申请号:NO20061751
申请日:2006-04-20
Applicant: STATOIL ASA
Inventor: PETTERSEN JOSTEIN , PAUROLA PENTTI , FREDHEIM ARNE OLAV , BAUER HEINZ , BOLT MANFRED , SAPPER RAINER , FRANKE HUBERT , SCHIER M
Abstract: A method of liquefying a hydrocarbon-rich gas, wherein the gas flows through a cascade of three refrigeration stages, each stage comprising a refrigerant circuit and a compressor, wherein at least part of the flow of refrigerant from the second circuit is used for the pre-cooling of the hydrocarbon rich gas in the first refrigeration stage. This balances the load on each of the compressors. By standardizing the drive units and compressors of the three coolant circuits, it is possible to maximize the attainable liquefaction capacity of the liquefaction process using tried-and-trusted drive units and compressors respectively. This method can be applied to mixed refrigerant cascades and circuits with a carbon dioxide pre-cooling circuit. This latter option has benefits for offshore use where large amounts of hydrocarbons are undesirable.
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公开(公告)号:NO20053282A
公开(公告)日:2006-01-09
申请号:NO20053282
申请日:2005-07-05
Applicant: STATOIL ASA
Inventor: STOCKMANN RUDOLF , BAUER HEINZ , PAUROLA PENTTI , SAPPER RAINER , FRANKE HUBERT
IPC: F25J1/00 , F25J20060101 , F25J1/02
CPC classification number: F25J1/0022 , F25J1/0042 , F25J1/0052 , F25J1/0055 , F25J1/0057 , F25J1/0214 , F25J1/0283 , F25J1/0287 , F25J1/0292 , F25J1/0295 , F25J1/0296 , F25J1/0298 , F25J2220/64 , F25J2245/02
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公开(公告)号:NO20050944A
公开(公告)日:2005-02-22
申请号:NO20050944
申请日:2005-02-22
Applicant: STATOIL ASA
Inventor: PAUROLA PENTTI , STOCKMANN RUDOLF , GWINNER MARTIN
CPC classification number: F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J3/0247 , F25J2200/30 , F25J2205/50 , F25J2215/64 , F25J2220/60 , F25J2245/02 , F25J2260/20 , F25J2270/90
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公开(公告)号:AU2003281633A8
公开(公告)日:2004-02-09
申请号:AU2003281633
申请日:2003-07-01
Applicant: LINDE AG , STATOIL ASA
Inventor: STOCKMANN RUDOLF , GWINNER MARTIN , PAUROLA PENTTI
Abstract: A process for liquefying a flow of natural gas with simultaneous recovery of a C 3 /C 4 -rich fraction is described, whereby the liquefaction of the flow of natural gas is carried out in heat exchange for at least one refrigerant and/or mixed refrigerant flow, and the flow of natural gas that is to be liquefied, after precooling, is subjected to a rectifying column, in which higher hydrocarbons are separated from the flow of natural gas, and then is subjected to further cooling and liquefaction, whereby a C 2+ -rich fraction that is recovered in the subsequent cooling of the flow of natural gas is fed to the rectifying column as a reflux liquid. According to the invention, a C 4 /C 5 -rich fraction ( 20, 35 ) is fed directly and/or indirectly to rectifying column (T 1 ) as an additional reflux liquid, whereby the feed point of the C 4 /C 5 -rich [fraction ( 20, 35 ) is located at the top of rectifying column (T 1 ) or is identical to the feed point of the C 2+ -rich fraction ( 5 ).]
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公开(公告)号:NO20034865D0
公开(公告)日:2003-10-31
申请号:NO20034865
申请日:2003-10-31
Applicant: STATOIL ASA
Inventor: BUTZ PETER , GWINNER MARTIN , STOCKMANN RUDOLF , PAUROLA PENTTI , JENSEN RUNE
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公开(公告)号:AU2003206897A1
公开(公告)日:2003-09-04
申请号:AU2003206897
申请日:2003-02-14
Applicant: LINDE AG , STATOIL ASA
Inventor: PAUROLA PENTTI , STOCKMANN RUDOLF , GWINNER MARTIN
Abstract: The invention relates to a method for compressing a multi-constituent flow, particularly a coolant mixture flow whereby, before compression, the multi-constituent flow is, inside a separating device, freed from liquid possibly contained in the multi-constituent flow to be compressed. According to the invention, a partial flow (5, 6, 8) of the compressed multi-component flow (3, 4) is fed at least occasionally to the separating device (D). The partial flow (5, 6, 8) fed to the separating device (D) can be diverted from the compressed multi-component flow (3, 4) before and/or after being subjected to a cooling (E) that ensues after compression (V).
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公开(公告)号:AU2004274706B2
公开(公告)日:2008-08-07
申请号:AU2004274706
申请日:2004-09-23
Applicant: LINDE AG , STATOIL ASA
Inventor: FRANKE HUBERT , PETTERSEN JOSTEIN , BOLT MANFRED , BAUER HEINZ , PAUROLA PENTTI , SCHIER MARC , SAPPER RAINER , FREDHEIM ARNE OLAV
Abstract: A method of liquefying a hydrocarbon-rich gas, wherein the gas flows through a cascade of three refrigeration stages, each stage comprising a refrigerant circuit and a compressor, wherein at least part of the flow of refrigerant from the second circuit is used for the pre-cooling of the hydrocarbon rich gas in the first refrigeration stage. This balances the load on each of the compressors. By standardizing the drive units and compressors of the three coolant circuits, it is possible to maximize the attainable liquefaction capacity of the liquefaction process using tried-and-trusted drive units and compressors respectively. This method can be applied to mixed refrigerant cascades and circuits with a carbon dioxide pre-cooling circuit. This latter option has benefits for offshore use where large amounts of hydrocarbons are undesirable.
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公开(公告)号:NO20061751A
公开(公告)日:2006-06-22
申请号:NO20061751
申请日:2006-04-20
Applicant: STATOIL ASA
Inventor: PETTERSEN JOSTEIN , PAUROLA PENTTI , FREDHEIM ARNE OLAV , BAUER HEINZ , BOLT MANFRED , SAPPER RAINER , FRANKE HUBERT , SCHIER M
CPC classification number: F25J1/0052 , F25B1/10 , F25B5/02 , F25B9/008 , F25B2309/06 , F25B2400/13 , F25J1/0022 , F25J1/0095 , F25J1/0217 , F25J1/0218 , F25J1/0278 , F25J1/0279 , F25J1/0283 , F25J1/0292 , F25J1/0295 , F25J1/0296 , F25J1/0297 , F25J2220/64
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公开(公告)号:DE102004032710A1
公开(公告)日:2006-02-09
申请号:DE102004032710
申请日:2004-07-06
Applicant: LINDE AG , STATOIL ASA STAVANGER
Inventor: BAUER HEINZ , FRANKE HUBERT , PAUROLA PENTTI , SAPPER RAINER , STOCKMANN RUDOLF
IPC: F25J20060101 , F25J1/00 , F25J1/02
Abstract: Method for liquefying a hydrocarbon-rich stream, especially a natural gas stream, comprises separating a first coolant mixture cycle (1-12) into a low boiling fraction (10) and a higher boiling fraction (2). The two fractions have different pressures and are fed to a pre-cooling unit (E1). Preferred Features: Pre-cooling of the hydrocarbon-rich stream is carried out in a wound heat exchanger. A second coolant mixture cycle (20-25) has a compressor (V2) with a pressure ratio of at least 10.
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