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公开(公告)号：US08685358B2
公开(公告)日：2014-04-01
申请号：US13116952
申请日：2011-05-26
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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: In various implementations, feed streams that include ultrapure, high-pressure hydrogen streams and ultrapure, high-pressure nitrogen streams are reacted to produce ultrapure, high-pressure feed gas in a stoichiometric ratio to an ammonia synthesis reactor loop without or independent of including a methanol loop purge gas.
Abstract translation: 在各种实施方案中，包括超纯水，高压氢气流和超纯高压氮气流的进料流被反应以产生与氨合成反应器回路的化学计量比的超纯高压进料气体，而不需要或独立地包括 甲醇循环吹扫气体。
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公开(公告)号：US08652223B2
公开(公告)日：2014-02-18
申请号：US12569694
申请日：2009-09-29
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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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公开(公告)号：US07988765B2
公开(公告)日：2011-08-02
申请号：US12390100
申请日：2009-02-20
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: B01D53/02
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 Fischer-Tropsch 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: 在各种实施方案中，可以处理包括氢气和一氧化碳的各种原料气流，以转化成产物流。 例如，进料气流可以使用费 - 托法或甲醇合成方法进行处理。 未转化的氢气和一氧化碳可以在高回收率和/或惰性成分被循环使用，以通过使用设计用于回收不纯的产物气流的变压吸附系统的布置来防止再循环系统中的积聚。
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公开(公告)号：US20100022668A1
公开(公告)日：2010-01-28
申请号：US12488377
申请日：2009-06-19
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: C07C1/04
CPC classification number: C07C1/0425 , C01B3/382 , C01B3/384 , C01B3/52 , C01B13/0229 , C01B2203/0233 , C01B2203/0244 , C01B2203/04 , C01B2203/0415 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0844 , C01B2203/0894 , C01B2203/1241 , C01B2203/1288 , C01B2203/141 , C01B2210/0046 , C07C1/041 , C10G2/32 , C10G2300/4081 , C10G2300/807 , Y02P20/129
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 Fischer-Tropsch process. Unconverted hydrogen and carbon monoxide can be recycled using an off-gas catalytic reformer and a gas turbine exhaust gas heat exchanger that will perform preheating duties.
Abstract translation: 在各种实施方案中，可以处理包括氢气和一氧化碳的各种原料气流，以转化成产物流。 例如，可以使用费 - 托方法处理进料气流。 未转化的氢气和一氧化碳可以使用废气催化重整器和将执行预热任务的燃气轮机排气热交换器进行再循环。
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公开(公告)号：US20090211442A1
公开(公告)日：2009-08-27
申请号：US12390100
申请日：2009-02-20
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: B01D53/047
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 Fischer-Tropsch 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: 在各种实施方案中，可以处理包括氢气和一氧化碳的各种原料气流，以转化成产物流。 例如，进料气流可以使用费 - 托法或甲醇合成方法进行处理。 未转化的氢气和一氧化碳可以在高回收率和/或惰性成分被循环使用，以通过使用设计用于回收不纯的产物气流的变压吸附系统的布置来防止再循环系统中的积聚。
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Patent Agency Ranking
公开(公告)号：US6030598A
公开(公告)日：2000-02-29
申请号：US93209
申请日：1998-06-08
Applicant: Anthony K. J. Topham , Rodney J. Allam
Inventor： Anthony K. J. Topham , Rodney J. Allam
IPC: B01D53/04 , B01D53/047 , C01B13/10 , B01D53/02
CPC classification number: C01B13/10 , B01D53/047 , B01D2253/108 , B01D2256/14 , B01D2257/104 , B01D2257/106 , B01D2259/40056 , B01D2259/40079 , B01D2259/40081 , B01D2259/403 , B01D53/0423
Abstract: An ozone containing gas stream is produced from oxygen by subjecting oxygen to an electric discharge and the ozone is then adsorbed on to a solid adsorbent, such as zeolite, the oxygen containing stream leaving the adsorbent is recycled to the ozonising process. Periodically, oxygen adsorbed on the adsorbent is desorbed by co-currently passing a purge gas over the adsorbent and the desorbed oxygen is also recycled to the ozoniser. Lastly ozone is desorbed from the adsorbent by a counter-current flow of purge gas and used in an ozone demanding process.
Abstract translation: 通过使氧进行放电，然后将臭氧吸附到诸如沸石的固体吸附剂上，由氧气产生含臭氧的气流，离开吸附剂的含氧流再循环到臭氧化过程中。 周期性地，吸附剂上吸附的氧气通过共同通过吹扫气体吸附在吸附剂上而解吸，并且解吸的氧也被再循环到臭氧发生器中。 最后，臭氧通过逆流净化气体从吸附剂中解吸并用于臭氧需求过程中。
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47.发明授权Use of nitrogen from an air separation plant in carbon dioxide removal from a feed gas to a further process 失效使用来自空气分离设备的氮气从进料气体中除去二氧化碳至另一种方法
公开(公告)号：US5582029A
公开(公告)日：1996-12-10
申请号：US538878
申请日：1995-10-04
Applicant: James M. Occhialini , Rodney J. Allam , Mohammed A. Kalbassi
Inventor： James M. Occhialini , Rodney J. Allam , Mohammed A. Kalbassi
CPC classification number: C21B13/14 , B01D53/0462 , B01D53/047 , B01D53/0476 , C21B13/0073 , C21B5/00 , F25J3/04539 , F25J3/04545 , F25J3/04557 , F25J3/04563 , F25J3/04587 , B01D2253/102 , B01D2253/104 , B01D2253/108 , B01D2257/504 , B01D2257/80 , B01D2259/40001 , B01D2259/40056 , B01D2259/40081 , B01D2259/402 , B01D2259/416 , B01D53/261 , C21B2100/02 , C21B2100/04 , F25J2205/66 , Y02C10/08 , Y02P10/122 , Y02P10/126 , Y02P10/128 , Y02P10/136 , Y02P10/216 , Y10S62/928
Abstract: A cryogenic air separation unit (ASU) provides flows of oxygen and nitrogen. The oxygen is used in a process such as COREX iron making or the partial oxidation of hydrocarbons, or in an oxycoal fuelled blast furnace, producing an off-gas containing useful components (H.sub.2 and CO) and carbon dioxide. The carbon dioxide is removed by pressure swing adsorption using nitrogen from the ASU as a regeneration gas and the purified off-gas becomes a feed gas to a further process such as production of iron by direct reduction of iron ore or the production of a NH.sub.3 making ammonia or is recycled into the first process as a feed gas.
Abstract translation: 低温空气分离装置（ASU）提供氧气和氮气流。 氧气用于诸如COREX制铁或烃的部分氧化，或者在氧化石燃料高炉中，产生含有有用组分（H 2和CO）和二氧化碳的废气。 通过使用来自ASU的氮作为再生气体通过变压吸附除去二氧化碳，并且净化的废气成为进一步的过程的进料气体，例如通过直接还原铁矿石或生产NH 3制备生产铁 氨或作为进料气循环进入第一工艺。
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公开(公告)号：US5483806A
公开(公告)日：1996-01-16
申请号：US439802
申请日：1995-05-12
Applicant: Jeremy P. Miller , Colin D. Smith , Rodney J. Allam , Anthony K. J. Topham
Inventor： Jeremy P. Miller , Colin D. Smith , Rodney J. Allam , Anthony K. J. Topham
CPC classification number: F25B9/004
Abstract: A refrigeration system using air as the refrigerant comprises a compressor which compresses air to 84 bar g. The compressed air is cooled first by cooling water and then by returning air in a plate-fin heat exchanger before being expanded to 59 bar g in an expander. The expanded air at -61.degree. C. is passed through indirect cooling coils in a cold store which it leaves at -45.degree. C. This air is then passed through the plate-fin heat exchanger before being recycled to the compressor. The refrigeration delivered is about 1.05 kw refrigeration/kw power input.
Abstract translation: 使用空气作为制冷剂的制冷系统包括将空气压缩至84巴g的压缩机。 首先通过冷却水冷却压缩空气，然后在膨胀器中膨胀至59巴g之前，通过在板翅式热交换器中返回空气。 在-61℃的膨胀空气在-45℃离开的冷库中通过间接冷却盘管。然后在将空气再循环到压缩机之前将该空气通过板翅式热交换器。 供应的制冷约为1.05 kw制冷/ kw功率输入。
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公开(公告)号：US5306331A
公开(公告)日：1994-04-26
申请号：US32885
申请日：1993-03-18
Applicant: Steven R. Auvil , Rodney J. Allam , Paul A. Webley , Philip J. Young
Inventor： Steven R. Auvil , Rodney J. Allam , Paul A. Webley , Philip J. Young
IPC: B01D53/047 , B01D53/22
CPC classification number: B01D53/047 , B01D53/226 , B01D53/229 , B01D2253/102 , B01D2253/108 , B01D2259/40001 , B01D53/0423
Abstract: The present invention provides a process for utilizing one stream from a gas separation unit in an evaporation cooler to provide cool water which is used to cool the feed gas mixture by direct or indirect contact prior to entering the gas separation unit.
Abstract translation: 本发明提供一种利用来自蒸发冷却器中的气体分离单元的一个流以提供冷水的方法，所述冷却水用于在进入气体分离单元之前通过直接或间接接触来冷却进料气体混合物。
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50.发明授权
公开(公告)号：US4871382A
公开(公告)日：1989-10-03
申请号：US187682
申请日：1988-04-29
Applicant: Robert M. Thorogood , Douglas L. Bennett , Rodney J. Allam , Alan L. Prentice , Bruce K. Dawson
Inventor： Robert M. Thorogood , Douglas L. Bennett , Rodney J. Allam , Alan L. Prentice , Bruce K. Dawson
CPC classification number: F25J3/04309 , F25J3/04206 , F25J3/04412 , F25J3/04678 , F25J3/04884 , F25J3/04909 , F25J3/04915 , B01J2219/326 , F25J2250/40 , F25J2250/50 , F25J2250/58 , F25J2290/10 , Y10S62/906 , Y10S62/924
Abstract: The present invention relates to an improvement to a cryogenic air separation process having an argon sidearm column. The improvement to the process for maximizing argon recovery comprises effectuating the intimate contact of the liquid phase stream and the vapor phase stream in the low pressure column and the argon sidearm column of an integrated multi-column, e.g. three column, cryogenic distillation system by utilizing a structured or ordered packing.
Abstract translation: 本发明涉及具有氩侧臂柱的低温空气分离方法的改进。 对于使氩回收最大化的方法的改进包括实现液相物流和集成多塔的低压塔和氩侧臂柱中的气相物流的紧密接触，例如， 三柱，低温蒸馏系统，利用结构或有序包装。
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