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    GENERATING POWER USING AN ION TRANSPORT MEMBRANE
    2.
    发明申请
    GENERATING POWER USING AN ION TRANSPORT MEMBRANE 审中-公开
    使用离子传输膜产生功率

    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.

    IPC: F02C6/18 ,  F02C3/20 ,  F02C7/00 ,  F01D15/10

    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。

    GENERATING POWER USING AN ION TRANSPORT MEMBRANE
    3.
    发明申请
    GENERATING POWER USING AN ION TRANSPORT MEMBRANE 审中-公开
    使用离子交换膜产生电力

    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.

    IPC: F02C3/20 ,  F02C6/18 ,  F02C7/00 ,  B01D59/30 ,  B01D61/38

    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。

    INCREMENTAL HYDROGEN PRODUCTION FROM AN EXISTING STEAM/NATURAL GAS REFORMER
    4.
    发明申请
    INCREMENTAL HYDROGEN PRODUCTION FROM AN EXISTING STEAM/NATURAL GAS REFORMER 审中-公开
    来自现有蒸汽/天然气改造者的增产氢

    公开(公告)号：WO2016187125A1

    公开(公告)日：2016-11-24

    申请号：PCT/US2016/032716

    申请日：2016-05-16

    Applicant: GTLPETROL, LLC

    Inventor： ALLAM, Rodney J.

    IPC: C01B3/56

    CPC classification number: C01B3/56 ,  B01D53/002 ,  B01D53/04 ,  B01D53/047 ,  B01D2256/16 ,  B01D2257/108 ,  B01D2257/504 ,  B01D2257/80 ,  B01D2259/41 ,  C01B2203/0205 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/0495 ,  C01B2203/062 ,  C01B2203/146 ,  C01B2203/147 ,  Y02C10/08 ,  Y02P20/152

    Abstract: In some aspects, a method for incremental hydrogen production includes separating in a first Pressure Swing Absorption (PSA) system an existing reformer synthesis gas product stream into a first hydrogen stream and a first waste stream. The first waste stream is compressed to at least 40 bar to produce a compressed waste stream. Water is removed from the compressed waste stream to produce a dried waste stream. Carbon dioxide is removed from the dried waste stream to produce a remaining waste stream, and the removed carbon dioxide is at least 85% of carbon dioxide in the existing reformer synthesis gas product stream. A second PSA system separates the remaining waste stream into a second hydrogen stream and a second waste stream, and the second hydrogen stream comprises at least 11% of hydrogen from the existing reformer synthesis gas product stream. The second waste stream is passed to a reformer furnace as fuel gas.

    Abstract translation: 在一些方面，用于增量氢气生产的方法包括在第一压力摆动吸收（PSA）系统中将现有的重整器合成气产物流分离成第一氢气流和第一废气流。 将第一废物流压缩至至少40巴以产生压缩废物流。 从压缩的废物流中除去水以产生干燥的废物流。 将二氧化碳从干燥的废物流中除去以产生剩余的废物流，并且所除去的二氧化碳在现有的重整器合成气产物流中为至少85％的二氧化碳。 第二PSA系统将剩余的废物流分离成第二氢气流和第二废物流，并且第二氢气流包含来自现有重整器合成气产物流的至少11％的氢气。 将第二废物流作为燃料气体送入重整炉。

    PRODUCING AMMONIA USING ULTRAPURE, HIGH PRESSURE HYDROGEN
    5.
    发明申请
    PRODUCING AMMONIA USING ULTRAPURE, HIGH PRESSURE HYDROGEN 审中-公开
    使用超声波，高压氢生产氨

    公开(公告)号：WO2011150253A1

    公开(公告)日：2011-12-01

    申请号：PCT/US2011/038205

    申请日：2011-05-26

    Applicant: GTLPETROL LLC ,  ALLAM, Rodney J.

    Inventor： ALLAM, Rodney J.

    IPC: C01B3/02 ,  C01B3/38 ,  C01B3/48 ,  C01B3/52 ,  C01B3/56

    CPC classification number: C01C1/0405 ,  C01B3/025 ,  C01B3/382 ,  C01B3/384 ,  C01B3/386 ,  C01B3/48 ,  C01B3/52 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/0288 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/068 ,  C01B2203/0844 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/86 ,  Y02P20/124 ,  Y02P20/52 ,  Y02P30/30

    Abstract: A system and method for producing ammonia, comprising: a partial oxidation reactor (POX) or an autothermal reforming reactor (ATR) that exothermically reacts a first portion of a hydrocarbon feed stream; a gas -heated catalytic reformer (GHR) that endothermically reforms a second portion of the hydrocarbon feed stream with steam over a catalyst and combines the exothermically generated syngas product and the endothermically- reformed syngas product; a first heat exchanger that cools the combined syngas stream to produce steam in a heat recovery boiler; one or more shift conversion reactors that catalytically reacts the combined syngas stream; a second heat exchanger that cools the shifted stream; a scrubber that removes C02 from the shifted syngas stream; one or more pressure swing adsorption systems that generate a high pressure, substantially pure H2 stream from the C02 -depleted stream; and an ammonia reactor (20) that combines the high pressure, substantially pure H2 stream with (30) a high pressure, substantially pure N2 stream (40) to produce ammonia (50).

    Abstract translation: 一种用于生产氨的系统和方法，包括：部分氧化反应器（POX）或自热重整反应器（ATR），其使烃进料流的第一部分放热反应; 一种气体加热催化重整器（GHR），其通过催化剂上的蒸汽将第二部分烃进料物流改造，并将放热产生的合成气产物和吸热重整合成气产物组合; 第一热交换器，其冷却合并的合成气流以在热回收锅炉中产生蒸汽; 一个或多个转化反应器，其将合并的合成气流催化反应; 第二个热交换器，冷却转移的流; 从移动的合成气流中除去CO 2的洗涤器; 一个或多个压力变动吸附系统，其从所述CO 2分离的流中产生高压，基本上纯的H 2流; 和氨反应器（20），其将高压，基本上纯的H 2流与（30）高压，基本上纯的N 2流（40）组合以产生氨（50）。

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