-
公开(公告)号：US20120056132A1
公开(公告)日：2012-03-08
申请号：US13195712
申请日：2011-08-01
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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。
-
公开(公告)号：US20110294907A1
公开(公告)日：2011-12-01
申请号：US13115780
申请日：2011-05-25
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
CPC classification number: C07C29/1518 , B01J19/0053 , B01J19/245 , B01J2219/00051 , B01J2219/00873 , B01J2219/00905 , B01J2219/0875 , B01J2219/24 , C01B3/36 , C01B3/382 , C01B3/384 , C01B13/0248 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/04 , C01B2203/0495 , C01B2203/061 , C01B2203/0844 , C01B2203/0894 , C01B2210/0046 , Y02P20/123 , Y02P20/124 , Y02P20/129 , C07C31/04
Abstract: In various implementations, methanol is produced using a (CO+H2) containing synthesis gas produced from a combined PDX plus EHTR or a combined ATR plus EHTR at a pressure of 70 bar to 100 bar at the correct stoichiometric composition for methanol synthesis so that no feed gas compressor is required for the feed to the methanol synthesis reactor loop.
Abstract translation: 在各种实施方案中，使用由组合的PDX加EHTR或组合的ATR plus EHTR产生的（CO + H 2）的合成气在70巴至100巴的压力下以合适的化学计量组成用于甲醇合成来生产甲醇，使得不 进料气压缩机是进料到甲醇合成反应器回路所必需的。
-
公开(公告)号：US20100263385A1
公开(公告)日：2010-10-21
申请号：US12763081
申请日：2010-04-19
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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 CO2 or fuel components CO and CH4 which contain carbon so that when combusted in a suitable gas turbine there may be minimal or reduced emissions of CO2 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 CO2 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。
-
公开(公告)号：US20100047160A1
公开(公告)日：2010-02-25
申请号：US12544099
申请日：2009-08-19
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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，包括甲烷的进料流反应产生合成气。 可以进一步处理合成气以产生超纯的高压氢气流。
-
公开(公告)号：US06360561B1
公开(公告)日：2002-03-26
申请号：US09798111
申请日：2001-03-02
Applicant: Rodney J. Allam , Declan P. O'Connor
Inventor： Rodney J. Allam , Declan P. O'Connor
IPC: F25J300
Abstract: High pressure gaseous oxygen is obtained safely and without compression by heating pumped liquid oxygen in a printed circuit type heat exchanger having layers of transversely extending laterally spaced channels with each layer being in thermal contact with at least one other layer. Oxygen is vaporized in channels of oxygen-layers against heat exchange fluid passing through channels of heat exchange layers. The walls of the oxygen layer channels are formed of ferrous alloy and have a cross-section, in a plane perpendicular to the direction of flow, having a thickness at its narrowest of at least about 10%, and on average at least about 15%, of the combined hydraulic mean diameters of the adjacent channels, and the ratio of cross-sectional area, in said plane, of the walls to the cross-sectional area of the channels is no less than about 0.7.
-
Patent Agency Ranking36.发明授权Control method to maximize argon recovery from cryogenic air separation units 失效从低温空气分离单元最大化氩回收的控制方法
公开(公告)号：US4842625A
公开(公告)日：1989-06-27
申请号：US187683
申请日：1988-04-29
Applicant: Rodney J. Allam , Alan L. Prentice
Inventor： Rodney J. Allam , Alan L. Prentice
IPC: F25J3/04
CPC classification number: F25J3/048 , F25J3/04206 , F25J3/04309 , F25J3/04412 , F25J3/04678 , F25J3/04884 , F25J2240/40 , F25J2245/40 , F25J2250/40 , F25J2250/50 , F25J2250/58 , Y10S62/924
Abstract: The present invention relates to an improvement to a conventional cryogenic air separation process having an argon sidearm column. The improvement to the process comprises reducing the pressure of the feed gas to the argon sidearm column across a control valve and operating the argon sidearm column at the lowest possible pressure consistent with a minimum temperature difference across the overhead condenser and the unrestricted return of crude oxygen vapor from the overhead condenser to the low pressure column.
-
公开(公告)号：US20140308172A1
公开(公告)日：2014-10-16
申请号：US14251122
申请日：2014-04-11
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: C10G2/00
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 syngas 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，其向具有相关功率和热量的费 - 托催化烃合成系统提供进料气体 能源系统
-
公开(公告)号：US20140283526A1
公开(公告)日：2014-09-25
申请号：US14294843
申请日：2014-06-03
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: F02C6/18
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 CO2 or fuel components CO and CH4 which contain carbon so that when combusted in a suitable gas turbine there may be minimal or reduced emissions of CO2 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 CO2 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。
-
公开(公告)号：US20140248205A1
公开(公告)日：2014-09-04
申请号：US14177535
申请日：2014-02-11
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
IPC: C01C1/04
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。
-
公开(公告)号：US08753427B2
公开(公告)日：2014-06-17
申请号：US13195712
申请日：2011-08-01
Applicant: Rodney J. Allam
Inventor： Rodney J. Allam
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。
-
-
-
-
-
-
-
-
-
Search Results
52
records
(took 0.02 seconds)
