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公开(公告)号：US08424308B2
公开(公告)日：2013-04-23
申请号：US12737810
申请日：2009-08-18
Applicant: Isabella Lodewina Greeff
Inventor： Isabella Lodewina Greeff
Abstract: A process (10) for co-producing synthesis gas and power includes in a synthesis gas generation stage, producing a hot synthesis gas and, in a nuclear power generation stage (12), heating a working fluid with heat generated by a nuclear reaction to produce a heated working fluid and generating power by expanding the heated working fluid using one or more turbines (16), with additional heating (14) of the heated working fluid by indirect transfer of heat from the hot synthesis gas to the heated working fluid.
Abstract translation: 用于共同生产合成气和功率的方法（10）包括在合成气生成阶段中，产生热合成气，并且在核发电阶段（12）中，通过核反应产生的热量加热工作流体至 通过使用一个或多个涡轮机（16）膨胀加热的工作流体并通过将热量从热合成气体间接转移到加热的工作流体来加热被加热的工作流体来产生加热的工作流体并发电。
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公开(公告)号：US20120067060A1
公开(公告)日：2012-03-22
申请号：US13322144
申请日：2010-05-20
Applicant: Isabella Lodewina Greeff
Inventor： Isabella Lodewina Greeff
IPC: F02C6/18
CPC classification number: C01B3/36 , B01D53/229 , B01D2256/12 , B01D2257/102 , C01B13/0251 , C01B2203/0211 , C01B2203/0227 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/061 , C01B2203/062 , C01B2203/0838 , C01B2203/1241 , C01B2203/84 , C01B2210/0046 , C10G2/32 , C10J3/00 , C10J2300/093 , C10J2300/0959 , C10J2300/0976 , C10J2300/1659 , C10J2300/1678 , C10J2300/1884 , F01K23/068 , F02C1/04 , F02C3/28 , G21D9/00 , Y02E20/18 , Y02P20/129
Abstract: A process for co-producing synthesis gas and power includes producing a synthesis gas comprising at least CO and H2 by reacting a hydrocarbonaceous feedstock with oxygen, the synthesis gas being at a first temperature, separating air from a compressed air stream by means of at least one ion transport membrane unit thereby producing a permeate stream consisting predominantly of oxygen and a reject stream of oxygen-depleted air at a second temperature which is lower than the first temperature, indirectly heating the reject stream of oxygen-depleted air with the synthesis gas and at least partially expanding, the heated reject stream of oxygen-depleted air through at least one turbine to generate power, producing an at least partially expanded reject stream of oxygen-depleted air, and feeding at least a portion of the permeate stream consisting predominantly of oxygen to the synthesis gas generation stage to provide oxygen for production of synthesis gas.
Abstract translation: 共同生产合成气和动力的方法包括通过使烃原料与氧气反应来生产至少包含CO和H 2的合成气，所述合成气处于第一温度，至少通过至少从压缩空气流中分离空气 一个离子传递膜单元，从而在低于第一温度的第二温度下产生主要由氧气和贫氧空气的排出流组成的渗透物流，间接地用合成气加热贫氧空气的废气流，以及 至少部分地膨胀经过至少一个涡轮的加热的贫氧气流，以产生动力，产生至少部分膨胀的贫氧空气的废气流，以及将至少一部分主要由 氧气到合成气生成阶段提供氧气生产合成气。
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公开(公告)号：US09021814B2
公开(公告)日：2015-05-05
申请号：US13322144
申请日：2010-05-20
Applicant: Isabella Lodewina Greeff
Inventor： Isabella Lodewina Greeff
IPC: F02C3/28 , C01B3/36 , B01D53/22 , C01B13/02 , C10G2/00 , C10J3/00 , F02C1/04 , F01K23/06 , G21D9/00
CPC classification number: C01B3/36 , B01D53/229 , B01D2256/12 , B01D2257/102 , C01B13/0251 , C01B2203/0211 , C01B2203/0227 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/061 , C01B2203/062 , C01B2203/0838 , C01B2203/1241 , C01B2203/84 , C01B2210/0046 , C10G2/32 , C10J3/00 , C10J2300/093 , C10J2300/0959 , C10J2300/0976 , C10J2300/1659 , C10J2300/1678 , C10J2300/1884 , F01K23/068 , F02C1/04 , F02C3/28 , G21D9/00 , Y02E20/18 , Y02P20/129
Abstract: A process for co-producing synthesis gas and power includes producing a synthesis gas comprising at least CO and H2 by reacting a hydrocarbonaceous feedstock with oxygen, the synthesis gas being at a first temperature, separating air from a compressed air stream by means of at least one ion transport membrane unit thereby producing a permeate stream consisting predominantly of oxygen and a reject stream of oxygen-depleted air at a second temperature which is lower than the first temperature, indirectly heating the reject stream of oxygen-depleted air with the synthesis gas and at least partially expanding, the heated reject stream of oxygen-depleted air through at least one turbine to generate power, producing an at least partially expanded reject stream of oxygen-depleted air, and feeding at least a portion of the permeate stream consisting predominantly of oxygen to the synthesis gas generation stage to provide oxygen for production of synthesis gas.
Abstract translation: 共同生产合成气和动力的方法包括通过使烃原料与氧气反应来生产至少包含CO和H 2的合成气，所述合成气处于第一温度，至少通过至少从压缩空气流中分离空气 一个离子传递膜单元，从而在低于第一温度的第二温度下产生主要由氧气和贫氧空气的排出流组成的渗透物流，间接地用合成气加热贫氧空气的废气流，以及 至少部分地膨胀经过至少一个涡轮的加热的贫氧气流，以产生动力，产生至少部分膨胀的贫氧空气的废气流，以及将至少一部分主要由 氧气到合成气生成阶段提供氧气生产合成气。
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Patent Agency Ranking
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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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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公开(公告)号：US08247462B2
公开(公告)日：2012-08-21
申请号：US12526672
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 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 synthesized (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，其中烃从合成气中合成（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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公开(公告)号：US20110131992A1
公开(公告)日：2011-06-09
申请号：US12737810
申请日：2009-08-18
Applicant: Isabella Lodewina Greeff
Inventor： Isabella Lodewina Greeff
Abstract: A process (10) for co-producing synthesis gas and power includes in a synthesis gas generation stage, producing a hot synthesis gas and, in a nuclear power generation stage (12), heating a working fluid with heat generated by a nuclear reaction to produce a heated working fluid and generating power by expanding the heated working fluid using one or more turbines (16), with additional heating (14) of the heated working fluid by indirect transfer of heat from the hot synthesis gas to the heated working fluid.
Abstract translation: 用于共同生产合成气和功率的方法（10）包括在合成气生成阶段中，产生热合成气，并且在核发电阶段（12）中，通过核反应产生的热量加热工作流体至 通过使用一个或多个涡轮机（16）膨胀加热的工作流体并通过将热量从热合成气体间接转移到加热的工作流体来加热被加热的工作流体来产生加热的工作流体并发电。
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公开(公告)号：US20100018217A1
公开(公告)日：2010-01-28
申请号：US12526822
申请日：2008-02-08
IPC: F02C6/00
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 (114) 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 (112) 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。 功率（114）由燃烧气体产生，包括在氧的存在下燃烧（78）燃烧气体，并且在至少一部分分离的CO 2存在下作为调节剂产生热的燃烧气体（106） 其中包括二氧化碳。 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螯合或捕获的CO 2排气流（134）。
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