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公开(公告)号:CA2506534C
公开(公告)日:2013-05-07
申请号:CA2506534
申请日:2003-11-10
Inventor: RYTTER ERLING , ERI SIGRID , SCHANKE DAG
Abstract: A catalyst for use in a Fischer-Tropsch synthesis reaction which comprises cobalt supported on alumina, in which: the catalyst average particle size is in the range 20 to 100 ~m; the specific surface area of the impregnated and calcined catalyst particles is greater than 80 m2/g; the average pore size of the impregnated and calcined catalyst is at least 90.ANG. (9nm); and the pore volume of the impregnated and calcined catalyst is greater than 0.35 cm3/g.
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公开(公告)号:CA2545879C
公开(公告)日:2011-09-20
申请号:CA2545879
申请日:2003-11-21
Applicant: STATOIL ASA
Inventor: EDWIN EMIL , ARNESEN TORE , AASER KNUT-IVAR , RYTTER ERLING , JOHANSEN JOHAN ARNOLD
Abstract: The invention provides a method for the conversion into carbon of gaseous hydrocarbons extracted from a natural hydrocarbon reservoir, which method comprises contacting said gaseous hydrocarbon at an elevated temperature in a reactor with a catalyst capable of converting said hydrocarbon to carbon and hydrogen; burning hydrogen produced by the conversion of the hydrocarbon, optionally after separating hydrogen produced from unconverted hydrocarbon, burning said hydrogen to generate energy; and using the energy generated to heat said reactor or the gaseous hydrocarbon flow thereto, or to heat or power a heat or power consuming apparatus.
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公开(公告)号:CA2509944C
公开(公告)日:2011-03-22
申请号:CA2509944
申请日:2002-12-13
Inventor: SHAW GARETH DAVID HUNTLEY , OLSVIK OLA , RYTTER ERLING , SOGGE JOSTEIN , STENSEN JAN AGE
Abstract: A method for increasing oil recovery from an oil reservoir in which method surplus gas streams from a plant for synthesis of higher hydrocarbons from natural gas is injected into the reservoir, is described. The surplus streams from the plant is the tailgas from the synthesis and optionally nitrogen from an air separation unit which delivers oxygen or oxygen enriched air to the plant for synthesis of higher hydrocarbons.
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公开(公告)号:AU2004293656B2
公开(公告)日:2010-03-04
申请号:AU2004293656
申请日:2004-11-22
Applicant: STATOIL ASA
Inventor: EDWIN EMIL , AASER KNUT-IVAR , JOHANSEN JOHAN ARNOLD , RYTTER ERLING , ARNESEN TORE , FORS JOHN
IPC: B01J8/00 , B01J8/02 , B01J8/12 , B01J8/24 , B01J8/28 , B01J19/02 , C01B3/00 , C01B3/26 , C01B31/02 , D01F9/127 , D01F9/133
Abstract: This invention relates to a method for the production of particulate carbon products in a reactor vessel wherein gas flow between a gas inlet port and a gas outlet port suspends a bed of catalyst-containing particulate material in said vessel and wherein the product is discharged from said vessel by falling from the bed.
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公开(公告)号:NO20090086L
公开(公告)日:2009-03-09
申请号:NO20090086
申请日:2009-01-06
Applicant: STATOIL ASA
Inventor: EDWIN EMIL , BRUSTAD MORTEN , AASER KNUT-IVAR , RYTTER ERLING , MIKKELSEN OYVIND , JOHANSEN JOHAN ARNOLD
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公开(公告)号:EA011042B1
公开(公告)日:2008-12-30
申请号:EA200600926
申请日:2003-11-21
Applicant: STATOIL ASA
Inventor: EDWIN EMIL , ARNESEN TORE , AASER KNUT-IVAR , RYTTER ERLING , JOHANSEN JOHAN ARNOLD
Abstract: Визобретениипредложенспособпревращенияв углеродгазообразныхуглеводородов, извлеченныхизприродногоместорожденияуглеводородов, включающийконтактуказанногогазообразногоуглеводородаприповышеннойтемпературев реакторес катализатором, способнымпревратитьуказанныйуглеводородв углероди водород; сжиганиеводорода, полученногоприконверсииуглеводорода, возможно, послеотделенияполученноговодородаотнепрореагировавшегоуглеводорода, причемсжиганиеуказанноговодородапредназначенодляполученияэнергии; ииспользованиеполученнойэнергиидлянагреванияуказанногореактораилипоступающегов негопотокагазообразногоуглеводорода, илидлянагреванияилиэнергоснабженияаппарата, потребляющеготеплоилиэнергию.
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公开(公告)号:DE60131471T2
公开(公告)日:2008-10-02
申请号:DE60131471
申请日:2001-05-03
Applicant: STATOIL ASA
Inventor: RYTTER ERLING
Abstract: A method of reforming a feed gas comprising natural gas and/or a prereformed natural gas, water vapour and an oxygen-containing gas in an autothermal reactor, characterised in that by the feed gas is first passed through a catalyst free zone in the reactor, in which zone the feed gas is partially combusted in an exothermic oxidation reaction and partially reformed, that the hot, partially combusted and reformed gas is led further through a catalyst bed for further reforming, so as to form a reformed gas stream, and that the reformed gas stream is separated into a first stream primarily containing H2 and a second, low hydrogen stream primarily containing CO2, water vapour and CO, any inert gases and some unconverted feed gas, by means of a membrane in the catalyst bed, which membrane is permeable to hydrogen. A reactor for implementing the method is also described.
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公开(公告)号:GB2410449B
公开(公告)日:2008-05-21
申请号:GB0401829
申请日:2004-01-28
Applicant: STATOIL ASA
Inventor: RYTTER ERLING , SKAGSETH TORILD HULSUND , WIGUM HANNE , SINCADU NONYAMEKO
IPC: B01J32/00 , B01J21/00 , B01J21/04 , B01J21/10 , B01J23/00 , B01J23/36 , B01J23/74 , B01J23/75 , B01J23/755 , B01J23/76 , B01J23/80 , B01J23/83 , B01J23/889 , B01J23/89 , B01J35/00 , B01J35/10 , B01J37/02 , B01J37/08 , C01B3/38 , C07C1/04 , C10G2/00 , C10G45/58 , C10G47/00
Abstract: A method of producing an alumina-supported catalyst for use in a Fischer-Tropsch synthesis reaction, which comprises: calcining an initial γ-alumina support material at a temperature of at least 550° C. to produce a modified alumina support material; impregnating the modified alumina support material with a source cobalt; calcining the impregnated support material at a temperature of 700° C. to 1200° C., and activating the catalyst.
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公开(公告)号:EA009572B1
公开(公告)日:2008-02-28
申请号:EA200500805
申请日:2003-11-10
Applicant: STATOIL ASA , PETROLEUM OIL & AMP GAS CORP O
Inventor: RYTTER ERLING , ERI SIGRID , SCHANKE DAG
IPC: B01J35/10 , B01J23/75 , B01J23/889 , B01J35/02 , C10G2/00
Abstract: Предлпгпетсякатализатордляиспользованияв процессесинтезаФишера-Тропша, содержащийкобальт, нанесенныйнаоксидалюминия, вкоторомсреднийразмерчастицкатализаторасоставляетот 20 до 100 мкм; удельнаяплощадьповерхностипропитанныхи прокаленныхчастицкатализаторабольшечем 80 м/г; среднийразмерпорпропитанногои прокаленногокатализаторасоставляетпоменьшеймере 90Å (9 нм) иобъемпорпропитанногои прокаленногокатализаторабольшечем 0,35 см/г.
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公开(公告)号:NO20075944L
公开(公告)日:2008-01-17
申请号:NO20075944
申请日:2007-11-19
Applicant: STATOIL ASA
Inventor: RYTTER ERLING , KOBRO HENRIK , KOEIJER GELEIN DE , SIVERTSEN BORGE RYGH
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