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公开(公告)号:US20100184872A1
公开(公告)日:2010-07-22
申请号:US12525070
申请日:2008-01-29
IPC分类号: B01J23/889 , B01J19/00 , B01J8/00 , C07C27/00
CPC分类号: B01J37/08 , B01J21/04 , B01J23/005 , B01J23/75 , B01J23/8896 , C10G2/332 , C10G2/342
摘要: A method of producing a catalyst for use in a Fischer-Tropsch synthesis reaction. The method comprises the steps of: impregnating a catalyst support material with an active cobalt catalyst component to form a catalyst precursor; and calcining the catalyst precursor in an atmosphere of a dry calcining gas.
摘要翻译: 一种制备用于费 - 托合成反应的催化剂的方法。 该方法包括以下步骤:用催化剂载体材料浸渍活性钴催化剂组分以形成催化剂前体; 并在干煅烧气体的气氛中煅烧催化剂前体。
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公开(公告)号:US09242229B2
公开(公告)日:2016-01-26
申请号:US13814905
申请日:2011-07-29
申请人: Manoj M. Koranne , Erling Rytter , Sigrid Eri , Oyvind Borg
发明人: Manoj M. Koranne , Erling Rytter , Sigrid Eri , Oyvind Borg
IPC分类号: B01J23/75 , B01J23/889 , B01J23/00 , B01J23/89 , B01J35/10 , B01J37/02 , B01J37/08 , B01J37/18 , C10G2/00 , C10G45/58 , C10G47/00 , C07C1/04 , B01J23/755 , B01J23/76 , B01J23/80
CPC分类号: B01J23/8896 , B01J23/005 , B01J23/75 , B01J23/8913 , B01J35/1014 , B01J35/1038 , B01J37/0201 , B01J37/088 , B01J37/18 , C07C1/0445 , C10G2/33 , C10G2/332 , C10G2/342 , C10G45/58 , C10G47/00 , C10G2300/1022 , C10G2300/703
摘要: A method of producing an aluminum oxide supported catalyst for use in a Fischer-Tropsch synthesis reaction, which comprises: spray-drying a slurry of γ-alumina and a source of a spinel forming metal to form a solid precursor material; calcining the precursor material to form a modified support material including a metal aluminate spinel; impregnating the modified alumina support material with a source of cobalt; calcining the impregnated support material, and activating the catalyst.
摘要翻译: 一种制备用于费 - 托合成反应的氧化铝载体催化剂的方法,其包括:喷雾干燥γ-氧化铝的浆料和尖晶石形成金属源以形成固体前体材料; 煅烧前体材料以形成包含金属铝酸盐尖晶石的改性载体材料; 用钴源浸渍改性氧化铝载体材料; 煅烧浸渍的载体材料,并活化催化剂。
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公开(公告)号:US20130210939A1
公开(公告)日:2013-08-15
申请号:US13817501
申请日:2011-08-17
IPC分类号: C10G3/00
CPC分类号: C10G3/62 , B01J23/005 , B01J23/75 , B01J23/94 , B01J33/00 , B01J35/023 , B01J35/1014 , B01J35/1038 , B01J38/10 , B01J38/12 , C07C1/045 , C07C2521/04 , C07C2523/36 , C07C2523/42 , C07C2523/75 , C07C2523/889 , C07C2523/89 , C10G2/332 , Y02P20/584 , Y02P30/20 , Y10S502/514 , Y10S502/518
摘要: A process for the regeneration of deactivated catalyst from a Fischer-Tropsch synthesis reactor, the catalyst being a supported cobalt catalyst. The process comprises the following steps: a withdrawal step, in which a portion of deactivated catalyst together with liquid hydrocarbon is withdrawn from the reactor; a concentration step, in which the concentration of the catalyst in the liquid hydrocarbon is increased; a calcination step, in which the deactivated catalyst composition is subjected to an oxidising gas to oxidise carbonaceous material contained in the deactivated catalyst in to gaseous oxides of the components of the carbonaceous material; and a reactivation step, in which the deactivated catalyst composition is reactivated to produced a regenerated catalyst.
摘要翻译: 一种从费 - 托合成反应器再生失活催化剂的方法,催化剂是负载型钴催化剂。 该方法包括以下步骤:其中一部分失活催化剂与液体烃一起从反应器中排出的抽出步骤; 浓缩步骤,其中液体烃中催化剂的浓度增加; 煅烧步骤,其中失活的催化剂组合物经受氧化气体以将失活的催化剂中所含的含碳材料氧化成含碳材料的组分的气态氧化物; 和再活化步骤,其中使失活催化剂组合物再活化以产生再生催化剂。
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公开(公告)号:US20120149787A1
公开(公告)日:2012-06-14
申请号:US13378581
申请日:2010-08-31
申请人: Erling Rytter , Sigrid Eri , Rune Myrstad , Odd Asbjørn Lindvåg
发明人: Erling Rytter , Sigrid Eri , Rune Myrstad , Odd Asbjørn Lindvåg
IPC分类号: B01J23/75 , B01J23/83 , B01J23/80 , B01J23/32 , C07C1/04 , B01J23/745 , B01J23/755 , B01J23/84 , B01J27/128 , B01J23/76 , B01J23/78
CPC分类号: B01J23/8913 , B01J21/04 , B01J23/75 , B01J23/80 , B01J23/8896 , B01J23/894 , B01J23/8953 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J37/0205 , B01J37/0207 , B01J37/10 , B01J37/12 , B01J37/14 , B01J37/16 , B01J37/18 , C10G2/331 , C10G2/332 , C10G2/342 , C10G2300/703 , Y10S502/524
摘要: A method of producing an alumina-supported cobalt catalyst for use in a Fischer-Tropsch synthesis reaction, which comprises: calcining an initial γ-alumina support material at a temperature to produce a modified alumina support material; impregnating the modified alumina support material with a source of cobalt; calcining the impregnated support material, activating the catalyst with a reducing gas, steam treating the activated catalyst, and activating the steam treated catalyst with a reducing gas.
摘要翻译: 一种制备用于费 - 托合成反应的氧化铝负载的钴催化剂的方法,其包括:在温度下煅烧初始γ-氧化铝载体材料以产生改性的氧化铝载体材料; 用钴源浸渍改性氧化铝载体材料; 煅烧浸渍的载体材料,用还原气体活化催化剂,蒸汽处理活化的催化剂,以及用还原气体活化蒸汽处理的催化剂。
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公开(公告)号:US20080064770A1
公开(公告)日:2008-03-13
申请号:US10535066
申请日:2003-11-10
申请人: Erling Rytter , Sigrid Eri , Dag Schanke
发明人: Erling Rytter , Sigrid Eri , Dag Schanke
CPC分类号: C10G2/332 , B01J23/75 , B01J23/8896 , B01J35/023 , B01J35/10 , B01J35/1019 , B01J35/1042 , B01J35/1061 , C10G2300/703
摘要: 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 μm; 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 Å (9 nm); and the pore volume of the impregnated and calcined catalyst is greater than 0.35 cm3g.
摘要翻译: 一种用于费 - 托合成反应的催化剂,其包含负载在氧化铝上的钴,其中:催化剂平均粒径在20-100μm的范围内; 浸渍和煅烧的催化剂颗粒的比表面积大于80m 2 / g; 浸渍和煅烧的催化剂的平均孔径至少为(9nm); 并且浸渍和煅烧的催化剂的孔体积大于0.35cm 3。
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公开(公告)号:US20100099780A1
公开(公告)日:2010-04-22
申请号:US12582541
申请日:2009-10-20
IPC分类号: C07C27/06
CPC分类号: C10G47/00 , B01J21/005 , B01J23/005 , B01J23/36 , B01J23/75 , B01J23/755 , B01J23/80 , B01J23/83 , B01J23/8896 , B01J23/8913 , B01J23/892 , B01J35/002 , B01J35/1014 , B01J35/109 , B01J35/1095 , B01J37/0205 , B01J37/0207 , C10G2/331 , C10G2/332 , C10G2/333 , C10G2/342 , C10G45/58 , C10G2300/703
摘要: 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.
摘要翻译: 一种制备用于费 - 托合成反应的氧化铝负载催化剂的方法,其包括:在至少550℃的温度下煅烧初始的γ-氧化铝载体材料,以制备改性的氧化铝载体材料; 用源钴浸渍改性氧化铝载体材料; 在700℃至1200℃的温度下煅烧浸渍的载体材料,并活化催化剂。
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公开(公告)号:US20100068123A1
公开(公告)日:2010-03-18
申请号:US12308039
申请日:2007-06-11
申请人: Emil Edwin , Morten Brustad , Knut-Ivar Aaser , Erling Rytter , Oyvind Mikkelsen , Johan Arnold Johansen
发明人: Emil Edwin , Morten Brustad , Knut-Ivar Aaser , Erling Rytter , Oyvind Mikkelsen , Johan Arnold Johansen
CPC分类号: D01F9/133 , B01J8/003 , B01J8/004 , B01J8/0045 , B01J8/085 , B01J8/10 , B01J19/02 , B01J2208/00176 , B01J2208/00203 , B01J2208/00212 , B01J2208/00309 , B01J2208/0053 , B01J2208/0084 , B01J2219/0218 , B01J2219/0286 , C01B32/05
摘要: This invention provides a reactor for carbon nano-fibre production comprising a generally horizontal elongate cylindrical reaction vessel arranged to rotate about its cylindrical axis and containing in use a particulate catalyst-containing reaction bed, said reaction vessel having a gas inlet port and a gas outlet port positioned such that one of said inlet and outlet ports is in said bed and the other is outside said bed.
摘要翻译: 本发明提供一种用于碳纳米纤维生产的反应器,其包括大致水平的细长圆柱形反应容器,其设置成围绕其圆柱轴线旋转并且在使用中包含含颗粒催化剂的反应床,所述反应容器具有气体入口和气体出口 端口定位成使得所述入口和出口中的一个位于所述床中,而另一个在所述床之外。
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公开(公告)号:US07677309B2
公开(公告)日:2010-03-16
申请号:US12122181
申请日:2008-05-16
IPC分类号: E21B43/00
CPC分类号: C10G2/32 , C01B3/382 , C01B2203/0244 , C01B2203/0283 , C01B2203/062 , C01B2203/0844 , C01B2203/1241 , C01B2203/142 , C01B2203/82 , C01B2203/84 , E21B43/168
摘要: 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.
摘要翻译: 描述了一种用于从储油器中提高采油量的方法,其中方法将来自用于合成来自天然气的高级烃的工厂的剩余气体流注入储存器。 来自植物的剩余物流是来自合成的尾气和任选的来自空气分离单元的氮气,其将氧气或富氧空气输送到用于合成高级烃的工厂。
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公开(公告)号:US20100047158A1
公开(公告)日:2010-02-25
申请号:US12532222
申请日:2008-03-18
申请人: Borre Borresen , Erling Rytter , Ingrid Aartun , Bente Krogh , Morten Ronnekleiv
发明人: Borre Borresen , Erling Rytter , Ingrid Aartun , Bente Krogh , Morten Ronnekleiv
CPC分类号: C01B3/16 , C01B3/38 , C01B3/382 , C01B3/508 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0425 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/142 , Y02E60/324
摘要: A method for production of hydrogen including reforming of a carbon comprising fuel is provided together with production plants adapted for obtaining hydrogen at lower temperatures and/or higher pressures and obtaining a CO2 rich rest gas stream. A reformer and a water gas shift reactor are also provided.
摘要翻译: 与生产工厂一起提供包括重整含碳燃料的氢气的方法,该生产设备适于在较低温度和/或更高的压力下获得氢气并获得富含CO 2的气体气流。 还提供了重整器和水煤气变换反应器。
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公开(公告)号:US07481275B2
公开(公告)日:2009-01-27
申请号:US10538418
申请日:2003-12-12
申请人: Ola Olsvik , Erling Rytter , Jostein Sogge , Jan Age Stensen
发明人: Ola Olsvik , Erling Rytter , Jostein Sogge , Jan Age Stensen
CPC分类号: E21B43/168 , E21B43/40 , F25J3/04539 , F25J3/04569 , F25J3/04575 , F25J3/04593
摘要: A method for increasing oil recovery from an oil reservoir by injection of gas into the reservoir, is described. The method comprises separation of air into an oxygen-rich fraction and a nitrogen-rich fraction, reformation of natural gas together with oxygen to produce a synthesis gas for production of methanol 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.
摘要翻译: 描述了一种通过将气体注入贮存器来提高从储油器获得油的方法。 该方法包括将空气分离成富氧馏分和富氮馏分,天然气与氧一起重整以产生用于生产甲醇或其它含氧烃或高级烃的合成气。 原料合成产物和来自合成的废气被分离出来,富氮馏分和至少一部分废气被注入到油藏中以增加从储层中的油回收。 还描述了用于执行该方法的设备。
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