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公开(公告)号：US20080146683A1
公开(公告)日：2008-06-19
申请号：US11908923
申请日：2006-03-17
CPC classification number: B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
Abstract: Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内 共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。 当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。
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公开(公告)号：US20080114083A1
公开(公告)日：2008-05-15
申请号：US11908916
申请日：2006-03-17
CPC classification number: C10G2/342 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , C10G2/32
Abstract: A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in a plurality of vertically extending horizontally spaced slurry channels inside a common reactor shell, the slurry channels being defined between vertically extending horizontally spaced divider walls or plates and each slurry channel having a height, width and breadth such that the height and breadth are much larger than the width. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in the slurry channels, thereby to form non-gaseous and/or gaseous product. Gaseous product and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相淤浆反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，浆料体包含在多个垂直延伸的水平间隔的浆料 通道在共同的反应器壳体内，浆液通道限定在垂直延伸的水平隔开的分隔壁或板之间，并且每个浆料通道具有高度，宽度和宽度，使得高度和宽度远大于宽度。 当气态反应物向上通过存在于浆料通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 允许气体产物和/或未反应的气态反应物在淤浆体上方的顶部空间中与淤浆体脱离。
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13.发明申请Supply of Steam and Hydrogen to a Process or Plant Producing Synthesis Gas 审中-公开将蒸气和氢气供应给生产合成气的工艺或工厂公开(公告)号：US20080035889A1
公开(公告)日：2008-02-14
申请号：US10590005
申请日：2005-02-14
Applicant: Andre Peter Steynberg
Inventor： Andre Peter Steynberg
IPC: C01B3/38
CPC classification number: C01B3/384 , B01J8/067 , B01J2208/00309 , C01B3/34 , C01B3/36 , C01B3/382 , C01B3/386 , C01B13/0229 , C01B2203/0205 , C01B2203/0233 , C01B2203/025 , C01B2203/04 , C01B2203/065 , C01B2203/0816 , C01B2203/0894 , C01B2203/1241 , C01B2203/1258 , C01B2203/127 , C01B2203/1604 , C01B2210/0046 , C10G2/32 , Y02P20/129
Abstract: A method of supplying steam and a hydrogen feedstock to a primary process for producing synthesis gas includes, in a reformer of a secondary process which comprises a plurality of catalyst containing reforming passages, combusting a fuel to heat all of the reforming passages, whilst producing a hot synthesis gas by reforming a hydrocarbonaceous gas in the presence of process steam in some of the catalyst containing reforming passages only. The hot synthesis gas is cooled to produce steam which is supplied to the primary process. The cooled synthesis gas is treated to produce a hydrogen feedstock which is supplied to the primary process. The reforming passages not producing hot synthesis gas are cooled by passing a cooling medium through them and the hot synthesis gas exiting some of the reforming passages is separated from the cooling medium exiting other reforming passages.
Abstract translation: 向生产合成气的初级方法提供蒸汽和氢气原料的方法包括在包含多个含有催化剂的重整通道的二次方法的重整器中，燃烧燃料以加热所有的重整通道，同时产生 在一些仅含催化剂的重整通道的过程蒸汽存在下重整含烃气体的热合成气。 热合成气被冷却以产生供应到主要工艺的蒸汽。 处理冷却的合成气以产生供应给初级工艺的氢气原料。 通过使冷却介质通过它们来冷却不产生热合成气的重整通道，离开一些重整通道的热合成气与离开其它重整通道的冷却介质分离。
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公开(公告)号：US06462098B1
公开(公告)日：2002-10-08
申请号：US09916657
申请日：2001-07-25
Applicant: Alex Philip Vogel , Andre Peter Steynberg , Peter Jacobus Van Berge
Inventor： Alex Philip Vogel , Andre Peter Steynberg , Peter Jacobus Van Berge
IPC: C07C2700
CPC classification number: C10G2/342 , B01J8/006 , B01J8/226 , B01J2208/00141 , B01J2208/00672 , C07C1/0455
Abstract: A process for producing liquid and, optionally, gaseous products from gaseous reactants feeds (18), at a low level, gaseous reactants into a slurry bed of solid catalyst particles (14) suspended in a suspension liquid. The gaseous reactants are allowed to react as they pass upwardly through the slurry bed (14), hereby to form liquid and, optionally, gaseous products. The reaction is catalyzed by the catalyst particles. Liquid product is separated from the catalyst particles by passing, in a filtration zone (22) within the slurry bed, liquid product through a filtering medium having a plurality of openings through which the liquid passes. The openings have a controlling dimension of x microns. The proportion of catalyst particles, which have a particle size smaller than x microns, in the slurry bed is less than 18% by volume based on the total volume of the catalyst in the slurry bed.
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公开(公告)号：US08552073B2
公开(公告)日：2013-10-08
申请号：US12526822
申请日：2008-02-08
IPC: C07C27/00
CPC classification number: C10J3/00 , C10G2/32 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/1606 , C10J2300/165 , C10J2300/1659 , C10J2300/1675 , C10J2300/1807 , C10K1/004 , C10K1/005 , C10K1/101 , C10K1/103 , C10K1/143 , C10K1/165 , C10K3/04 , Y02E20/18 , Y02P20/129
Abstract: A process (10) for co-producing power and hydrocarbons includes gasifying (16, 70) coal to produce a synthesis gas (36) and a combustion gas (86) both comprising at least CO1H2 and CO2 and being at elevated pressure, separating CO2 (18, 48) from the synthesis gas, and synthesizing (20, 22) hydrocarbons from the synthesis gas. Power (1 14) is generated from the combustion gas, including by combusting (78) the combustion gas in the presence of oxygen and in the presence of at least a portion of the separated CO2 as moderating agent to produce a hot combusted gas (106) which includes CO2. The CO2 is recycled (1 12) or recovered from the combusted gas. In certain embodiments, the process (10) produces a CO2 exhaust stream (134) for sequestration or capturing for further use.
Abstract translation: 用于共同生产动力和烃的方法（10）包括气化（16,70）煤以产生合成气（36）和至少包括CO 1 H 2和CO 2并处于升高压力的燃烧气体（86），分离CO 2 （18,48），并从合成气中合成（20,22）烃。 燃烧气体产生动力（114），包括在氧的存在下燃烧（78）燃烧气体，并在至少一部分分离的CO 2存在下作为调节剂产生热燃气（106 ），其中包括CO2。 二氧化碳被回收（112）或从燃烧的气体中回收。 在某些实施方案中，方法（10）产生用于进一步使用的用于封存或捕获的CO 2排气流（134）。
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Patent Agency Ranking
公开(公告)号：US20130071293A1
公开(公告)日：2013-03-21
申请号：US13629179
申请日：2012-09-27
CPC classification number: B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
Abstract: Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内 共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。 当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。
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公开(公告)号：US08283386B2
公开(公告)日：2012-10-09
申请号：US13213640
申请日：2011-08-19
IPC: C07C27/00
CPC classification number: B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
Abstract: Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内 共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。 当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。
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公开(公告)号：US08013025B2
公开(公告)日：2011-09-06
申请号：US11908916
申请日：2006-03-17
IPC: C07C27/00
CPC classification number: C10G2/342 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , C10G2/32
Abstract: A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in a plurality of vertically extending horizontally spaced slurry channels inside a common reactor shell, the slurry channels being defined between vertically extending horizontally spaced divider walls or plates and each slurry channel having a height, width and breadth such that the height and breadth are much larger than the width. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in the slurry channels, thereby to form non-gaseous and/or gaseous product. Gaseous product and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相淤浆反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，浆料体包含在多个垂直延伸的水平间隔的浆料 通道在共同的反应器壳体内，浆液通道限定在垂直延伸的水平隔开的分隔壁或板之间，并且每个浆料通道具有高度，宽度和宽度，使得高度和宽度远大于宽度。 当气态反应物向上通过存在于浆料通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 允许气体产物和/或未反应的气态反应物在淤浆体上方的顶部空间中与浆料体脱离。
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公开(公告)号：US08008359B2
公开(公告)日：2011-08-30
申请号：US11908923
申请日：2006-03-17
IPC: C07C27/00
CPC classification number: B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
Abstract: Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内 共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。 当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。
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公开(公告)号：US20100022666A1
公开(公告)日：2010-01-28
申请号：US12526672
申请日：2008-02-08
IPC: C07C1/04
CPC classification number: C10J3/00 , C10G2/32 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/1606 , C10J2300/165 , C10J2300/1659 , C10J2300/1675 , C10J2300/1807 , C10K1/004 , C10K1/005 , C10K1/101 , C10K1/103 , C10K1/143 , C10K1/165 , C10K3/04 , Y02E20/18 , Y02P20/129
Abstract: A process (10) for co-producing power and hydrocarbons includes in a wet gasification stage (70), gasifying coal to produce a combustion gas (86) at elevated pressure comprising at least H2 and CO; enriching (72) a first portion of the combustion gas with H2 to produce an H2-enriched gas (88); and generating power (77) from a second portion of the combustion gas. In a dry gasification stage (16), coal is gasified to produce a synthesis gas precursor (36) at elevated pressure comprising at least H2 and CO. At least a portion of the H2-enriched gas (88) is mixed with the synthesis gas precursor (36) to provide a synthesis gas for hydrocarbon synthesis, with hydrocarbons being synthesised (20, 22) from the synthesis gas. In certain embodiments, the process (10) produces a CO2 exhaust stream (134) for sequestration or capturing for further use.
Abstract translation: 用于共同生产动力和烃的方法（10）包括在湿气化阶段（70）中，气化煤以产生包括至少H 2和CO的升高的燃烧气体（86）; 用H2富集（72）燃烧气体的第一部分以产生富H2的气体（88）; 以及从燃烧气体的第二部分产生动力（77）。 在干燥气化阶段（16）中，煤被气化以在包括至少H 2和CO的升高的压力下产生合成气前体（36）。至少部分富H2的气体（88）与合成气 前体（36）以提供用于烃合成的合成气，其中烃从合成气合成（20,22）。 在某些实施方案中，方法（10）产生用于进一步使用的用于封存或捕获的CO 2排气流（134）。
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