公开(公告)号：US06497811B1

公开(公告)日：2002-12-24

申请号：US09661053

申请日：2000-09-13

申请人： Trond Myrstad ,  Bente Boe ,  Erling Rytter ,  Hege Engan ,  Avelino Corma ,  Fernando Rey

发明人： Trond Myrstad ,  Bente Boe ,  Erling Rytter ,  Hege Engan ,  Avelino Corma ,  Fernando Rey

IPC分类号： C10G1100

CPC分类号： C10G29/06 ,  B01J23/002 ,  B01J23/06 ,  B01J23/74 ,  B01J2523/00 ,  C10G11/04 ,  C10G25/003 ,  B01J2523/22 ,  B01J2523/27 ,  B01J2523/31 ,  B01J2523/828

摘要： The present invention comprises a composition for reducing the sulphur content in a hydrocarbon composition, wherein the composition comprises a hydrotalcite material, which has been impregnated with a Lewis acid, and optionally a FCC-catalyst. The hydrotalcite material impregnated with the Lewis acid has been added as a separate component, or incorporated in the matrix of the FCC-catalyst. The Lewis acid is selected from the group comprising elements and compounds of the transition metals, and preferably Zn, Cu, Ni, Co, Fe and Mn, most preferably Zn. Further, the Lewis acid may also be selected from the group comprising elements and compounds of the lanthanides and actinides. The present invention also comprises a method for reducing the sulphur content in a hydrocarbon composition. A method for reducing the sulphur content in a hydrocarbon composition, which is to be cracked, is also described. Further, the use of a composition comprising a hydrotalcite material, which has been impregnated with a Lewis acid and optionally, mixed with a FCC-catalyst, is also included.

摘要翻译： 本发明包括用于降低烃组合物中硫含量的组合物，其中该组合物包含已经用路易斯酸和任选的FCC-催化剂浸渍的水滑石材料。 用路易斯酸浸渍的水滑石材料已经作为单独的组分加入，或者加入到FCC催化剂的基质中。 路易斯酸选自元素和过渡金属化合物，优选Zn，Cu，Ni，Co，Fe和Mn，最优选Zn。 此外，路易斯酸还可以选自元素和镧系元素和锕系元素的化合物。 本发明还包括一种降低烃组合物中硫含量的方法。 还描述了一种用于降低待裂化的烃组合物中的硫含量的方法。 此外，还包括使用已经浸渍有路易斯酸并任选地与FCC-催化剂混合的水滑石材料的组合物。

公开(公告)号：US5422375A

公开(公告)日：1995-06-06

申请号：US21783

申请日：1993-02-24

申请人： Erling Rytter ,  Petter Lian ,  Trond Myrstad ,  Per T. Roterud ,  Age Solbakken

发明人： Erling Rytter ,  Petter Lian ,  Trond Myrstad ,  Per T. Roterud ,  Age Solbakken

IPC分类号： B01D29/11 ,  B01D36/00 ,  B01J8/00 ,  B01J8/22 ,  C07C1/04 ,  C07C1/06 ,  C07C29/152 ,  C10G2/00

CPC分类号： B01D29/115 ,  B01J8/006 ,  B01J8/22 ,  C07C1/06 ,  C07C29/152 ,  C10G2/342 ,  B01D36/001 ,  Y02P20/52

摘要： A method of conducting a continuous multi-phase catalytic reaction such as the conversion of syngas to higher hydrocarbon fuels. Gaseous reactants are introduced via a gas permeable plate into a slurry which includes the product and a finely divided catalyst. The liquid product is separated from the remainder of the slurry by means of a filter unit including a filter member. A pressure differential is established across the filter member by means of a constant level device within the filter unit which maintains a level of filtrate within the filter unit below the level of the slurry. The slurry is maintained in a constant state of agitation by the introduction of the gaseous components as a steam of bubbles. Fluctuations in the pressure differential across the filter member prevent the filter member from clogging, and the gas space is above the filtrate and the slurry are in communication.

公开(公告)号：US08143186B2

公开(公告)日：2012-03-27

申请号：US11663663

申请日：2005-09-23

申请人： Erling Rytter

发明人： Erling Rytter

IPC分类号： B01J23/00 ,  B01J21/00 ,  B01J29/00 ,  B01J37/00 ,  B01J20/00

CPC分类号： B01J23/8896 ,  B01J21/04 ,  B01J21/06 ,  B01J23/005 ,  B01J23/75 ,  B01J23/755 ,  B01J35/1014 ,  B01J35/1019 ,  B01J37/0201 ,  C10G2/332 ,  C10G2300/703 ,  Y10S502/524

摘要： A catalyst composition comprising cobalt as an active catalytic element and a lesser amount of nickel as a promoter supported on a metal oxide support. The support may comprise alumina, silica, silica-alumina, zeolite, zirconia, magnesia or titania. The amount of nickel is preferably less than 50 wt %, relative to the amount of cobalt.

摘要翻译： 一种催化剂组合物，其包含钴作为活性催化元素，较少量的镍作为负载在金属氧化物载体上的催化剂。 载体可以包括氧化铝，二氧化硅，二氧化硅 - 氧化铝，沸石，氧化锆，氧化镁或二氧化钛。 相对于钴的量，镍的量优选小于50重量％。

公开(公告)号：US07827804B2

公开(公告)日：2010-11-09

申请号：US11911976

申请日：2006-04-19

申请人： Gelein De Koeijer ,  Erling Rytter ,  Børge Rygh Sivertsen ,  Henrik Kobro

发明人： Gelein De Koeijer ,  Erling Rytter ,  Børge Rygh Sivertsen ,  Henrik Kobro

IPC分类号： F02C6/18

CPC分类号： C01B3/384 ,  C01B3/48 ,  C01B3/56 ,  C01B13/0251 ,  C01B32/50 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2210/0046 ,  Y02P20/128

摘要： A process for production of electric energy and CO2 from a hydrocarbon feedstock includes steams reforming of the feedstock, separation and combustion of hydrogen and separation of CO2.

摘要翻译： 从烃原料生产电能和二氧化碳的方法包括原料的蒸汽重整，氢的分离和燃烧以及CO 2的分离。

公开(公告)号：US20080283254A1

公开(公告)日：2008-11-20

申请号：US12122181

申请日：2008-05-16

申请人： Gareth David Huntley Shaw ,  Ola Olsvik ,  Erling Rytter ,  Jostein Sogge ,  Jan Age Stensen

发明人： Gareth David Huntley Shaw ,  Ola Olsvik ,  Erling Rytter ,  Jostein Sogge ,  Jan Age Stensen

IPC分类号： E21B43/16

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。

公开(公告)号：US20070154382A1

公开(公告)日：2007-07-05

申请号：US10580231

申请日：2004-11-22

申请人： Emil Edwin ,  Tore Arnesen ,  Knut-Ivar Aaser ,  Erling Rytter ,  Johan Johansen ,  John Fors

发明人： Emil Edwin ,  Tore Arnesen ,  Knut-Ivar Aaser ,  Erling Rytter ,  Johan Johansen ,  John Fors

IPC分类号： B01J8/18 ,  B01J8/10 ,  D01F9/12

CPC分类号： D01F9/1272 ,  B01J4/002 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0055 ,  B01J8/006 ,  B01J8/009 ,  B01J8/0264 ,  B01J8/0278 ,  B01J8/12 ,  B01J8/125 ,  B01J8/24 ,  B01J8/28 ,  B01J19/02 ,  B01J2208/00176 ,  B01J2208/00415 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/0218 ,  B01J2219/185 ,  B01J2219/1941 ,  B01J2219/1943 ,  B01J2219/1946 ,  B82Y30/00 ,  C01B3/0021 ,  C01B3/26 ,  C01B32/05 ,  D01F9/127 ,  D01F9/1271 ,  D01F9/1273 ,  D01F9/1278 ,  D01F9/133 ,  Y02E60/325 ,  Y10S977/843

摘要： 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 the vessel and wherein the product is discharged from the vessel by falling from the bed.

摘要翻译： 一种用于在反应器容器中生产颗粒状碳产物的方法，其中在气体入口和气体出口之间的气体流将悬浮在容器中的含催化剂的颗粒材料床，并且其中产物从容器中排出， 床。

公开(公告)号：US20070140933A1

公开(公告)日：2007-06-21

申请号：US11467209

申请日：2006-08-25

申请人： Charles Besecker ,  Terry Mazanec ,  Sherman Xu ,  Erling Rytter

发明人： Charles Besecker ,  Terry Mazanec ,  Sherman Xu ,  Erling Rytter

IPC分类号： B01J8/02

CPC分类号： B01D69/141 ,  B01D53/228 ,  B01D71/024 ,  B01D2325/26 ,  B01J12/007 ,  B01J19/2475 ,  C01B3/386 ,  C01B13/0255 ,  C01B2203/0261 ,  C01B2203/1029 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2210/0046 ,  C01B2210/0053 ,  Y02P20/52

摘要： An apparatus for separating oxygen from an oxygen-containing gas and facilitating a chemical reaction with the separated oxygen includes a mixed conducting membrane, a porous body, and a material for catalyzing the reaction. The mixed conducting membrane has respective oxidation and reduction surfaces and is made of a non-porous, gas-impermeable, solid material capable of simultaneously conducting oxygen ions and electrons. At least the membrane and the catalyzing material are non-reactive with each other or are physically separated from each other during oxygen separation and the chemical reaction. The apparatus can be embodied by tubes, and a plurality of such tubes can form part of a reaction vessel in which various chemical reactions can occur benefiting from the apparatus design.

摘要翻译： 用于从含氧气体中分离氧气并促进与分离的氧气的化学反应的装置包括混合导电膜，多孔体和用于催化反应的材料。 混合导电膜具有相应的氧化和还原表面，并且由能够同时传导氧离子和电子的无孔气体不可渗透的固体材料制成。 至少膜和催化材料在氧分离和化学反应期间彼此不反应或者彼此物理分离。 该装置可以由管子实现，并且多个这样的管可以形成反应容器的一部分，其中可以从设备设计中获益各种化学反应。

公开(公告)号：US07168488B2

公开(公告)日：2007-01-30

申请号：US10487785

申请日：2002-08-30

申请人： Ola Olsvik ,  Erling Rytter ,  Jostein Sogge ,  Rune Kvale ,  Sjur Haugen ,  Jan Grøntvedt

发明人： Ola Olsvik ,  Erling Rytter ,  Jostein Sogge ,  Rune Kvale ,  Sjur Haugen ,  Jan Grøntvedt

IPC分类号： E21B43/18 ,  E21B43/34

CPC分类号： F25J3/04569 ,  C01B3/34 ,  C01B2203/0205 ,  C01B2203/0244 ,  C01B2203/0283 ,  C07C29/1518 ,  C10G2/30 ,  E21B43/168 ,  F25J3/04533 ,  F25J3/04539 ,  F25J3/04575 ,  F25J3/04593 ,  C07C31/04

摘要： 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.

摘要翻译： 公开了一种用于同时生产用于注入油田的气体并生产甲醇，二甲醚和/或其它含氧烃或从天然气生产高级烃的方法和设备。 用于生产注射纯氮的空气分离装置（ATR）和通过天然气的天然气改造生产合成气（“合成气”）的纯氧是该方法和装置的重要部分。

公开(公告)号：US20050003960A1

公开(公告)日：2005-01-06

申请号：US10495701

申请日：2002-11-14

申请人： Erling Rytter ,  Morten Ronnekleiv

发明人： Erling Rytter ,  Morten Ronnekleiv

IPC分类号： B01J23/00 ,  B01J23/62 ,  B01J35/00 ,  B01J37/00 ,  B01J37/02 ,  B01J37/03 ,  C07C5/333 ,  B01J23/755

CPC分类号： B01J37/0009 ,  B01J23/007 ,  B01J23/626 ,  B01J35/0006 ,  B01J37/0201 ,  B01J37/0221 ,  B01J37/03 ,  C07C5/3337 ,  C07C2521/04 ,  C07C2523/02 ,  C07C2523/14 ,  C07C2523/42 ,  Y02P20/52 ,  C07C11/06

摘要： The invention provides a formed heterogeneous catalyst composition comprising a particulate MII(MIII)O (wherein MII and MIII are divalent and trivalent metals respectively) catalyst support and a particulate binder wherein the surface area per unit weight of the support is greater than that of said binder and wherein the compressability of said binder is less than that of said support.

摘要翻译： 本发明提供了一种形成的非均相催化剂组合物，其包含颗粒M II（M III）O（其中M II和M III分别是二价和三价金属）催化剂载体和颗粒粘合剂，其中表面积 每单位重量的载体大于所述粘合剂的单位重量，并且其中所述粘合剂的可压缩性小于所述载体的可压缩性。

公开(公告)号：US06696501B2

公开(公告)日：2004-02-24

申请号：US10149060

申请日：2002-09-19

申请人： Dag Schanke ,  Roger Hansen ,  Jostein Sogge ,  Karina Heitnes Hofstad ,  Margrete H. Wesenberg ,  Erling Rytter

发明人： Dag Schanke ,  Roger Hansen ,  Jostein Sogge ,  Karina Heitnes Hofstad ,  Margrete H. Wesenberg ,  Erling Rytter

IPC分类号： C07C2700

CPC分类号： C10G2/32 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/043 ,  C01B2203/062 ,  C01B2203/0844 ,  C01B2203/0894 ,  C01B2203/1052 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/127 ,  C01B2203/141 ,  C01B2203/143 ,  C01B2203/146 ,  C01B2203/148 ,  C01B2203/82 ,  C07C1/0485

摘要： 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.

摘要翻译： 描述了将天然气或其他化石燃料转化为高级烃的方法，其包括以下步骤：a）在至少一个重整区中天然气与蒸汽和含氧气体的反应，以便产生主要由氢组成的合成气 和CO，除了一些二氧化碳; b）将所述合成气送入费 - 托反应器，以产生由低级烃，水和未转化的合成气组成的粗合成料流; c）将回收区中的所述粗合成物流分离成主要含有较重烃的粗产物流，主要含有剩余组分的水流和尾气流; 其特征在于该方法还包括以下步骤： d）在单独的蒸汽重整器中重新形成尾气中的至少一部分; e）在将其引入费 - 托反应器之前，将重整后的尾气引入气流中。