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公开(公告)号：WO2012051315A2
公开(公告)日：2012-04-19
申请号：PCT/US2011/055983
申请日：2011-10-12
Applicant: GTLPETROL, LLC , ALLAM, Rodney J.
Inventor： ALLAM, Rodney J.
CPC classification number: F02C3/20 , F01K23/10 , F02C3/28 , F02C3/30 , F02C6/06 , F02C6/18 , F02C7/141 , F02C7/22 , F05D2220/32 , F05D2220/722 , F05D2220/75 , F05D2240/24 , F05D2240/35 , Y02E20/16 , Y02E20/18 , Y02E50/11 , Y02E50/12
Abstract: In some implementations, a system may include a compressor, a heat exchanger and an ITM. The compressor is configured to receive an air stream and compress the air stream to generate a pressurized stream. The heat exchanger is configured to receive the pressured stream and indirectly heat the pressurized stream using heat from an oxygen stream from an Ion Transport Membrane (ITM). The ITM is configured to receive the heated pressurized stream and generate an oxygen stream and the non-permeate stream, wherein the non-permeate stream is passed to a gas turbine burner and the oxygen stream is passed to the heat exchanger.
Abstract translation: 在一些实现中，系统可以包括压缩机，热交换器和ITM。 压缩机被构造成接收气流并压缩气流以产生加压流。 热交换器构造成接收加压流并利用来自离子迁移膜（ITM）的氧流的热量间接加热加压流。 ITM被配置为接收经加热的加压流并产生氧气流和非渗透物流，其中非渗透物流被传送到燃气轮机燃烧器并且氧气流被传送到热交换器。
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公开(公告)号：WO2012009575A2
公开(公告)日：2012-01-19
申请号：PCT/US2011/044078
申请日：2011-07-14
Applicant: GTLPETROL LLC , ALLAM, Rodney J.
Inventor： ALLAM, Rodney J.
CPC classification number: F02C7/22 , C01B13/0251 , C01B2203/84 , F02C3/28 , F02C3/30 , F02C6/06 , F02C6/10 , F02C6/18 , F02C7/00 , F05D2220/722 , F05D2220/75 , F05D2260/213 , F05D2270/20 , Y02E20/16 , Y02E20/18 , Y02E50/11 , Y02E50/12
Abstract: In some implementations, a system may include a compressor, a heat exchanger and an ITM. The compressor is configured to receive an air stream and compress the air stream to generate a pressurized stream. The heat exchanger is configured to receive the pressured stream and indirectly heat the pressurized stream using heat from an oxygen stream from an Ion Transport Membrane (ITM). The ITM is configured to receive the heated pressurized stream and generate an oxygen stream and the non-permeate stream, wherein the non-permeate stream is passed to a gas turbine burner and the oxygen stream is passed to the heat exchanger.
Abstract translation: 在一些实施方式中，系统可以包括压缩机，热交换器和ITM。 压缩机构造成接收气流并压缩空气流以产生加压流。 热交换器被配置为接收加压流并且使用来自离子输送膜（ITM）的氧气流的热量间接加热加压流。 ITM被配置为接收加热的加压流并产生氧气流和非渗透物流，其中非渗透物流被传送到燃气涡轮燃烧器，并且氧气流被传递到热交换器。
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公开(公告)号：WO2010121260A1
公开(公告)日：2010-10-21
申请号：PCT/US2010/031626
申请日：2010-04-19
Applicant: GTLPETROL LLC , ALLAM, Rodney J.
Inventor： ALLAM, Rodney J.
CPC classification number: C01B3/34 , B01J19/24 , C01B3/36 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/50 , C01B3/56 , C01B2203/0233 , C01B2203/025 , C01B2203/0283 , C01B2203/0288 , C01B2203/042 , C01B2203/0475 , C01B2203/0844 , C01B2203/0872 , C01B2203/1235 , C01B2203/1241 , C01B2203/1294 , C01B2203/141 , C01B2203/82 , C01B2203/84 , C01B2203/86 , F02C6/18 , Y02E20/14 , Y02E20/16 , Y02P20/129 , Y02P30/30
Abstract: In some implementations, one or more methods can include producing a hydrogen rich fuel gas for a gas turbine ballasted with nitrogen and steam and superheated to a temperature above its dew point. The fuel gas may have a minimal or reduced content of CO 2 or fuel components CO and CH 4 which contain carbon so that when combusted in a suitable gas turbine there may be minimal or reduced emissions of CO 2 to the atmosphere. These example methods may result in a capture of the bulk of the carbon present in the total natural gas feed as CO 2 compressed to pipeline delivery pressure for sequestration.
Abstract translation: 在一些实施方案中，一种或多种方法可以包括为用氮气和蒸汽镇压的燃气轮机产生富氢燃料气体，并过热至高于其露点的温度。 燃料气体可以具有包含碳的二氧化碳或燃料组分CO和CH 4的最小或减少的含量，使得当在合适的燃气轮机中燃烧时，CO 2的排放可能最小化或减少到大气中。 这些示例性方法可以导致捕获总天然气进料中存在的大部分碳，因为二氧化碳被压缩成管道输送压力以用于螯合。
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4.发明申请
公开(公告)号：WO2010022162A2
公开(公告)日：2010-02-25
申请号：PCT/US2009/054332
申请日：2009-08-19
Applicant: GTLPETROL LLC , ALLAM, Rodney, J.
Inventor： ALLAM, Rodney, J.
CPC classification number: C01B3/382 , B01J2208/00309 , B01J2208/0053 , B01J2219/00006 , C01B3/48 , C01B3/56 , C01B3/583 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0255 , C01B2203/0283 , C01B2203/0288 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/068 , C01B2203/0805 , C01B2203/0872 , C01B2203/0894 , C01B2203/1217 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/146 , C01B2203/148 , C01B2203/1623 , C01B2203/1642 , C01B2203/86 , Y02E20/185 , Y02P30/30
Abstract: In various implementations, feed streams that include methane are reacted to produce synthesis gas. The synthesis gas may be further processed to produce ultrapure, high-pressure hydrogen streams.
Abstract translation: 在各种实施方案中，包括甲烷的进料流被反应以产生合成气。 可以进一步处理合成气以产生超纯的高压氢气流。
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公开(公告)号：WO2010037093A3
公开(公告)日：2010-07-22
申请号：PCT/US2009058769
申请日：2009-09-29
Applicant: GTLPETROL LLC , ALLAM RODNEY J
Inventor： ALLAM RODNEY J
CPC classification number: C01B3/38 , C01B3/36 , C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/0844 , C01B2203/0894 , C01B2203/1235 , C01B2203/1241 , C01B2203/1258 , C01B2203/1282 , C01B2203/141 , C01B2203/82 , Y02P20/129 , Y02P20/142
Abstract: In various systems and processes, synthesis gas generation may be combined. A partial oxidation reactor (POX) and a gas convectively heated steam/hydrocarbon catalytic reformer (GHR) may be combined to produce synthesis gas. In some implementations, a partial oxidation reactor, a gas convectively heated steam/catalytic reformer, and a waste hat boiler may be combined to produce synthesis gas.
Abstract translation: 在各种系统和方法中，可以组合合成气生成。 可以组合部分氧化反应器（POX）和气体对流加热的蒸汽/烃催化重整器（GHR）以产生合成气。 在一些实施方案中，可以组合部分氧化反应器，气体对流加热的蒸汽/催化重整器和废帽式锅炉，以产生合成气。
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Patent Agency Ranking
公开(公告)号：WO2010022162A3
公开(公告)日：2010-05-14
申请号：PCT/US2009054332
申请日：2009-08-19
Applicant: GTLPETROL LLC , ALLAM RODNEY J
Inventor： ALLAM RODNEY J
CPC classification number: C01B3/382 , B01J2208/00309 , B01J2208/0053 , B01J2219/00006 , C01B3/48 , C01B3/56 , C01B3/583 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0255 , C01B2203/0283 , C01B2203/0288 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/068 , C01B2203/0805 , C01B2203/0872 , C01B2203/0894 , C01B2203/1217 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/146 , C01B2203/148 , C01B2203/1623 , C01B2203/1642 , C01B2203/86 , Y02E20/185 , Y02P30/30
Abstract: In various implementations, feed streams that include methane are reacted to produce synthesis gas. The synthesis gas may be further processed to produce ultrapure, high-pressure hydrogen streams.
Abstract translation: 在各种实施方式中，包含甲烷的进料流反应以产生合成气。 合成气可以进一步处理以产生超纯的高压氢气流。
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公开(公告)号：WO2009105664A3
公开(公告)日：2009-12-03
申请号：PCT/US2009034704
申请日：2009-02-20
Applicant: GTLPETROL LLC , ALLAM RODNEY J
Inventor： ALLAM RODNEY J
CPC classification number: C10K1/26 , C01B3/36 , C01B3/56 , C01B2203/0244 , C01B2203/025 , C01B2203/043 , C01B2203/0465 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0495 , C01B2203/061 , C01B2203/062 , C01B2203/146 , C01B2203/148 , C10G2/32 , C10J3/00 , C10J2300/1659 , C10K1/20 , C10K1/32
Abstract: In various implementations, various feed gas streams which include hydrogen and carbon monoxide may be processed for conversion to product streams. For example, the feed gas stream may be processed using the Fisher-Tropsh process or a methanol synthesis process. Unconverted hydrogen and carbon monoxide can be recycled at high recovery and/or inert components removed to prevent build-up in the recycle system by using an arrangement of pressure swing adsorption systems designed to recover impure product gas streams.
Abstract translation: 在各种实施方式中，可以处理包括氢和一氧化碳的各种进料气流以转化成产物流。 例如，原料气流可以使用Fisher-Tropsh工艺或甲醇合成工艺进行处理。 未转化的氢气和一氧化碳可以高回收率和/或惰性组分回收利用，以防止在回收系统中积聚，这是通过使用设计用于回收不纯产品气流的变压吸附系统来实现的。
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公开(公告)号：WO2017075564A1
公开(公告)日：2017-05-04
申请号：PCT/US2016/059647
申请日：2016-10-31
Applicant: GTLPETROL, LLC
Inventor： ALLAM, Rodney J.
IPC: C01B3/50 , B01D53/047
CPC classification number: C01B3/506 , B01D53/002 , B01D53/047 , B01D53/75 , B01D53/864 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2257/80 , B01D2259/416 , C01B3/12 , C01B3/50 , C01B3/56 , C01B2203/0283 , C01B2203/042 , C01B2203/046 , C01B2203/0475 , C01B2203/147 , Y02C10/08
Abstract: The GTLpetrol Process for Maximum H2 Production. The GTLpetrol process uses a proprietary combination of two stage pressure swing adsorption hydrogen purification plus a C02 condensation removal step to give H2 recoveries in the range of 95% to 98% based on H2 + CO from synthesis gas generation.
Abstract translation:
用于最大H2生产的GTLpetrol过程。 所述GTLpetrol过程使用的两级变压吸附氢气提纯加一个CO 2冷凝除去工序的专有组合基于H 2 + CO合成气生成，得到H2回收率在95％至98％的范围内。
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9.发明申请
公开(公告)号：WO2014169219A1
公开(公告)日：2014-10-16
申请号：PCT/US2014/033818
申请日：2014-04-11
Applicant: GTLPETROL LLC
Inventor： ALLAM, Rodney J.
CPC classification number: C10G2/34 , B01D53/1475 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0894 , C01B2203/1241 , C01B2203/1294 , C01B2203/142 , C01B2203/148 , C01B2203/84 , C10G2300/4043 , C10K3/06 , Y02P20/152
Abstract: An integrated plant for the conversion of a hydrocarbon gas such as natural gas to useful hydrocarbon liquid fuels and feed-stocks comprises an H2+CO syn-gas generation system which provides feed gas to a Fischer-Tropsch catalytic hydrocarbon synthesis system with an associated power and heat energy system.
Abstract translation: 用于将天然气等烃类气体转化为有用的烃类液体燃料和原料的综合设备包括H2 + CO合成气生成系统，其向具有相关功率的费 - 托催化烃合成系统提供进料气体 和热能系统。
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公开(公告)号：WO2013033711A1
公开(公告)日：2013-03-07
申请号：PCT/US2012/053685
申请日：2012-09-04
Applicant: GTLPETROL LLC , ALLAM, Rodney J.
Inventor： ALLAM, Rodney J.
CPC classification number: B01D3/34 , B01D53/1406 , B01D53/1475 , B01D53/1487 , B01D2252/205 , B01D2257/702 , C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/043 , C01B2203/0495 , C01B2203/062 , C01B2203/0833 , C01B2203/0894 , C01B2203/1258 , C01B2203/141 , C01B2203/148 , C10G2300/1022 , C10K1/143 , Y02P20/152
Abstract: In some implementations, a method for separating components includes receiving off-gas from a Fischer-Tropsch hydrocarbon synthesis reaction process. The off-gas is scrubbed with a light oil at least proximate atmospheric temperature to substantially remove a mixture of C 3 and C 4 . The C 3 and C 4 are separated from the mixture into two separate streams using distillation columns in a Fischer-Tropsch system.
Abstract translation: 在一些实施方案中，用于分离组分的方法包括从费 - 托烃合成反应过程接收废气。 废气用至少接近大气温度的轻油擦洗，以基本上除去C3和C4的混合物。 使用费 - 托系统中的蒸馏塔将C3和C4从混合物分离成两个分开的流。
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