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公开(公告)号:CA2458634A1
公开(公告)日:2003-03-06
申请号:CA2458634
申请日:2002-08-30
Applicant: STATOIL ASA
Inventor: OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , KVALE RUNE , GRONTVEDT JAN , HAUGEN SJUR
Abstract: A method and a plant for simultaneous production of a gas for injection into an oil field and production of methanol, dimethyl ether and/or other oxygenated hydrocarbons or production of higher hydrocarbons from natural ga s is disclosed. An air separation unit (ATR) for production of pure nitrogen f or injection and pure oxygen for production of synthesis gas ("syngas") by authermal reformation of a natural gas is an essential part of the method an d plant.
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公开(公告)号:CA2458634C
公开(公告)日:2011-08-02
申请号:CA2458634
申请日:2002-08-30
Applicant: STATOIL ASA
Inventor: OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , KVALE RUNE , HAUGEN SJUR , GRONTVEDT JAN
Abstract: A method and a plant for simultaneous production of a gas for injection into an oil field and production of methanol, dimethyl ether and/or other oxygenated hydrocarbons or production of higher hydrocarbons from natural gas is disclosed. An air separation unit (ATR) for production of pure nitrogen for injection and pure oxygen for production of synthesis gas ("syngas") by authermal reformation of a natural gas is an essential part of the method and plant.
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公开(公告)号:AT406341T
公开(公告)日:2008-09-15
申请号:AT02731021
申请日:2002-06-27
Applicant: STATOIL ASA
Inventor: HANSEN ROGER , SOGGE JOSTEIN , VELAND BJORN , OLSVIK OLA
IPC: C07C29/151 , C07C29/152
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公开(公告)号:DE60215372D1
公开(公告)日:2006-11-23
申请号:DE60215372
申请日:2002-08-30
Applicant: STATOIL ASA
Inventor: OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , KVALE RUNE , HAUGEN SJUR , GRONTVEDT JAN
Abstract: A method and a plant for simultaneous production of a gas for injection into an oil field and production of methanol, dimethyl ether and/or other oxygenated hydrocarbons or production of higher hydrocarbons from natural gas is disclosed. An air separation unit (ATR) for production of pure nitrogen for injection and pure oxygen for production of synthesis gas ("syngas") by authermal reformation of a natural gas is an essential part of the method and plant.
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公开(公告)号:AT342427T
公开(公告)日:2006-11-15
申请号:AT02758957
申请日:2002-08-30
Applicant: STATOIL ASA
Inventor: OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , KVALE RUNE , HAUGEN SJUR , GRONTVEDT JAN
Abstract: A method and a plant for simultaneous production of a gas for injection into an oil field and production of methanol, dimethyl ether and/or other oxygenated hydrocarbons or production of higher hydrocarbons from natural gas is disclosed. An air separation unit (ATR) for production of pure nitrogen for injection and pure oxygen for production of synthesis gas ("syngas") by authermal reformation of a natural gas is an essential part of the method and plant.
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公开(公告)号:AU783540B2
公开(公告)日:2005-11-10
申请号:AU3248601
申请日:2000-12-28
Applicant: STATOIL ASA
Inventor: SOGGE JOSTEIN , BAHR LINDA , VELAND BJORN JARLE , OLSVIK OLA
IPC: C01B3/36 , C01B3/38 , C01B3/56 , C07C29/151 , C07C41/01
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27.
公开(公告)号:EA005458B1
公开(公告)日:2005-02-24
申请号:EA200400090
申请日:2002-06-27
Applicant: STATOIL ASA
Inventor: HANSEN ROGER , SOGGE JOSTEIN , VELAND BJORN JARLE , OLSVIK OLA
IPC: C07C29/151 , C07C29/152
Abstract: Описанспособувеличенияпроизводительностисуществующейтехнологическойустановкидляпревращенияприродногогазав продукт, вкоторойв синтез-газизсекциисинтез-газаподаютобогащенныйводородомпотокизразделенногопродувочногогаза, иэтотобогащенныйводородомсинтез-газпропускаютчерездополнительныйпроточныйреактордляполученияпродукта, атакжечерезблокдляотделенияобогащенногопродуктомпотока, которыйотбирают, ипотокас низкимсодержаниемпродукта, которыйиспользуютв качествесырьядляисходногореактора, причемв потокс низкимсодержаниемпродукта, которыйиспользуютв качествесырьядляисходногореактора, подаютдополнительныйсинтез-газ, полученныйв отдельнойлиниивторичногосинтез-газа.
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公开(公告)号:EA005448B1
公开(公告)日:2005-02-24
申请号:EA200400251
申请日:2002-08-30
Applicant: STATOIL ASA
Inventor: OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , KVALE RUNE , HAUGEN SJUR , GRONTVEDT JAN
Abstract: Предложеныспособи устройстводляодновременногополучениягазадлянагнетанияв нефтяноеместорождениеи дляполученияметанола, диметиловогоэфираи/илидругихкислородсодержащихуглеводородов, илиполучениявысшихуглеводородовизприродногогаза. Существеннойчастьюспособаи устройстваявляетсявоздухоразделительнаяустановка (ВРУ) дляполучениячистогоазотадлянагнетанияи чистогокислородадляполучениясинтез-газа ("синтетическогогаза") путёмавтотермическогореформингаприродногогаза.
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公开(公告)号:CA2509945A1
公开(公告)日:2004-07-01
申请号:CA2509945
申请日:2003-12-12
Applicant: STATOIL ASA
Inventor: STENSEN JAN ANG , SOGGE JOSTEIN , OLSVIK OLA , RYTTER ERLING
Abstract: A method for increasing oil recovery from an oil reservoir by injection of g as into the reservoir, is described. The method comprises separation of air int o an oxygen-rich fraction and a nitrogen-rich fraction, reformation of natural gas together with oxygen to produce a synthesis gas for production of methan ol or other oxygenated hydrocarbons or higher hydrocarbons. The raw synthesis products and a waste gas from the synthesis are separated, and the nitrogen- rich fraction and at least a part of the waste gas are injected into the oil reservoir to increase the oil recovery from the reservoir. A plant for performing the method is also described.
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公开(公告)号:ZA200204552B
公开(公告)日:2003-10-01
申请号:ZA200204552
申请日:2002-06-06
Applicant: STATOIL ASA
Inventor: SCHANKE DAG , SOGGE JOSTEIN , WESENBERG MARGRETE H , HANSEN ROGER , HOFSTAD KARINA HEITNES , RYTTER ERLING
Abstract: A method is described for conversion of natural gas or other fossil fuels to higher hydrocarbons, comprising the following steps: a) reaction of natural gas with steam and oxygenic gas in at least one reforming zone in order to produce a synthesis gas consisting primarily of hydrogen and CO, in addition to some carbon dioxide; b) passing said synthesis gas to a Fisher-Tropsch reactor in order to produce a crude synthesis stream consisting of lower hydrocarbons, water and non-converted synthesis gas; c) separation of said crude synthesis stream in a recovery zone, into a crude product stream mainly containing heavier hydrocarbons, a water stream and a tail gas stream mainly containing the remaining constituents; which is charaterized in that the method also comprises the following steps; d) stream reformation of at least part of the tail gas in a separate steam reformer; e) introduction of the reformed tail gas into the gas stream before this is led into the Fischer-Tropsch reactor.
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