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1.发明授权公开(公告)号：US09227844B2
公开(公告)日：2016-01-05
申请号：US13522341
申请日：2011-01-18
Applicant: Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
Inventor： Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
CPC classification number: C01B3/384 , B01J8/067 , B01J2208/00212 , B01J2208/00221 , B01J2208/00371 , B01J2208/0053 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0844 , C01B2203/0877 , C01B2203/1235 , C01B2203/142
Abstract: The invention relates to a process and apparatus for the production of synthesis gas from a hydrocarbon feedstock in a heat exchanger reformer, wherein a cooling medium is added to the heat exchange reformer.
Abstract translation: 本发明涉及一种用于在热交换器重整器中从烃原料生产合成气的方法和装置，其中向热交换重整器中加入冷却介质。
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公开(公告)号：US20090184293A1
公开(公告)日：2009-07-23
申请号：US12335363
申请日：2008-12-15
Applicant: Pat A. Han
Inventor： Pat A. Han
IPC: C01B3/38
CPC classification number: C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0816 , C01B2203/0833 , C01B2203/1241 , C01B2203/143
Abstract: The invention relates to a process for the production of synthesis gas from a hydrocarbon feedstock, wherein the entire hydrocarbon feed is passed through a radiant furnace, heat exchanger reformer and autothermal reformer in a series arrangement, and in which effluent gas from the autothermal reformer is used as heat source for the reforming reactions occurring in the heat exchange reformer.
Abstract translation: 本发明涉及从烃原料生产合成气的方法，其中整个烃进料以串联方式通过辐射炉，热交换器重整器和自热重整器，其中来自自热重整器的废气是 用作热交换重整器中发生的重整反应的热源。
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公开(公告)号：US08696935B2
公开(公告)日：2014-04-15
申请号：US13522919
申请日：2011-01-18
Applicant: Niklas Bengt Jakobsson , Anders Helbo Hansen , Pat A. Han
Inventor： Niklas Bengt Jakobsson , Anders Helbo Hansen , Pat A. Han
CPC classification number: B01J8/062 , B01J8/067 , B01J12/007 , B01J2208/00212 , B01J2208/00504 , B01J2219/0004 , B01J2219/00094 , B01J2219/00157 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0816 , C01B2203/0844 , C01B2203/0883 , C01B2203/1235 , C01B2203/143 , Y02P20/124
Abstract: The invention relates to a process for the production of synthesis gas from a hydrocarbon feedstock, wherein the entire hydrocarbon feed is passed through a radiant furnace, heat exchanger reformer and autothermal reformer in a series arrangement, in which effluent gas from the autothermal reformer is used as heat source for the reforming reactions occurring in the heat exchange reformer and wherein a cooling medium is added to the heat exchange reformer.
Abstract translation: 本发明涉及从烃原料生产合成气的方法，其中整个烃进料以串联方式通过辐射炉，热交换器重整器和自热重整器，其中使用来自自热重整器的废气 作为在热交换重整器中发生的重整反应的热源，并且其中向热交换重整器中加入冷却介质。
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公开(公告)号：US20130095029A1
公开(公告)日：2013-04-18
申请号：US13806729
申请日：2011-05-13
Applicant: Pat A. Han
Inventor： Pat A. Han
IPC: C01C1/04
CPC classification number: C01C1/0488 , C01B3/025 , C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/043 , C01B2203/0475 , C01B2203/061 , C01B2203/068 , C07C1/0485 , C07C29/1518 , Y02P20/52 , Y02P30/30 , C07C31/04
Abstract: Process for the co-production of methanol and ammonia from a hydrocarbon feed without venting to the atmosphere carbon dioxide captured from the methanol or ammonia synthesis gas and without using expensive air separation units, water gas shift and acid gas wash for removal of carbon.
Abstract translation: 从烃进料共同生产甲醇和氨的方法，而不排放到从甲醇或氨合成气中捕获的大气中的二氧化碳，并且不使用昂贵的空气分离单元，水煤气变换和用于除去碳的酸性气体洗涤。
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公开(公告)号：US20120326090A1
公开(公告)日：2012-12-27
申请号：US13522919
申请日：2011-01-18
Applicant: Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
Inventor： Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
IPC: C01B3/38
CPC classification number: B01J8/062 , B01J8/067 , B01J12/007 , B01J2208/00212 , B01J2208/00504 , B01J2219/0004 , B01J2219/00094 , B01J2219/00157 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0816 , C01B2203/0844 , C01B2203/0883 , C01B2203/1235 , C01B2203/143 , Y02P20/124
Abstract: The invention relates to a process for the production of synthesis gas from a hydrocarbon feedstock, wherein the entire hydrocarbon feed is passed through a radiant furnace, heat exchanger reformer and autothermal reformer in a series arrangement, in which effluent gas from the autothermal reformer is used as heat source for the reforming reactions occurring in the heat exchange reformer and wherein a cooling medium is added to the heat exchange reformer.
Abstract translation: 本发明涉及从烃原料生产合成气的方法，其中整个烃进料以串联方式通过辐射炉，热交换器重整器和自热重整器，其中使用来自自热重整器的废气 作为在热交换重整器中发生的重整反应的热源，并且其中向热交换重整器中加入冷却介质。
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Patent Agency Ranking
公开(公告)号：US08692034B2
公开(公告)日：2014-04-08
申请号：US13806729
申请日：2011-05-13
Applicant: Pat A. Han
Inventor： Pat A. Han
CPC classification number: C01C1/0488 , C01B3/025 , C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/043 , C01B2203/0475 , C01B2203/061 , C01B2203/068 , C07C1/0485 , C07C29/1518 , Y02P20/52 , Y02P30/30 , C07C31/04
Abstract: Process for the co-production of methanol and ammonia from a hydrocarbon feed without venting to the atmosphere carbon dioxide captured from the methanol or ammonia synthesis gas and without using expensive air separation units, water gas shift and acid gas wash for removal of carbon.
Abstract translation: 从烃进料共同生产甲醇和氨的方法，而不排放到从甲醇或氨合成气中捕获的大气中的二氧化碳，并且不使用昂贵的空气分离单元，水煤气变换和用于除去碳的酸性气体洗涤。
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公开(公告)号：US08303923B2
公开(公告)日：2012-11-06
申请号：US12626222
申请日：2009-11-25
Applicant: Pat A. Han
Inventor： Pat A. Han
CPC classification number: C01C1/0405 , C01B3/382 , C01B2203/0233 , C01B2203/025 , C01B2203/061 , C01B2203/068 , C01B2203/1241 , C01C1/0488 , C07C29/1518 , Y02P20/52 , C07C31/04
Abstract: Process for the co-production of methanol and ammonia from a hydrocarbon feed without venting to the atmosphere carbon dioxide captured from the methanol or ammonia synthesis gas and without using expensive air separation units, water gas shift and carbon dioxide removal steps.
Abstract translation: 用于从烃进料共同生产甲醇和氨的方法，而不排放到从甲醇或氨合成气中捕获的大气中的二氧化碳，并且不使用昂贵的空气分离单元，水煤气变换和二氧化碳去除步骤。
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公开(公告)号：US20120277327A1
公开(公告)日：2012-11-01
申请号：US13522341
申请日：2011-01-18
Applicant: Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
Inventor： Pat A. Han , Niklas Bengt Jakobsson , Anders Helbo Hansen
CPC classification number: C01B3/384 , B01J8/067 , B01J2208/00212 , B01J2208/00221 , B01J2208/00371 , B01J2208/0053 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0844 , C01B2203/0877 , C01B2203/1235 , C01B2203/142
Abstract: The invention relates to a process and apparatus for the production of synthesis gas from a hydrocarbon feedstock in a heat exchanger reformer, wherein a cooling medium is added to the heat exchange reformer.
Abstract translation: 本发明涉及一种用于在热交换器重整器中从烃原料生产合成气的方法和装置，其中向热交换重整器中加入冷却介质。
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公开(公告)号：US08261700B2
公开(公告)日：2012-09-11
申请号：US13000786
申请日：2009-06-17
Applicant: Henrik Otto Stahl , Pat A. Han
Inventor： Henrik Otto Stahl , Pat A. Han
IPC: F22G3/00
CPC classification number: C01C1/0405 , C01B3/025 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/52 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/068 , C01B2203/0811 , C01B2203/0844 , C01B2203/0894 , C01B2203/1241 , C01B2203/1258 , C01B2203/141 , C01C1/0452 , C01C1/0488 , F22B1/1838 , F28D7/0075 , F28D7/06 , F28F9/26 , Y02P20/129 , Y02P20/52
Abstract: Process for the production of ammonia from a hydrocarbon feedstock all steam produced in the waste heat boilers of the reforming and ammonia section of the plant is superheated in one or more steam superheaters located downstream the ammonia converter in the ammonia section of the plant. There is no need for steam superheater (s) in the reforming section of the plant to cool the synthesis gas. A steam superheater for use in the process is also provided. The superheater comprises two compartments in which the first and second compartments are connected in series with respect to the steam flow and in parallel with respect to the process gas flow.
Abstract translation: 用于从烃原料生产氨的方法在设备的氨部分中的氨转化器下游的一个或多个蒸汽过热器中过热在废气热锅炉中产生的所有蒸汽的重整和氨段的蒸汽过热。 在工厂的重整部分不需要蒸汽过热器来冷却合成气。 还提供了用于该过程的蒸汽过热器。 过热器包括两个室，其中第一和第二隔室相对于蒸汽流串联连接并且相对于处理气体流平行连接。
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公开(公告)号：US20110104037A1
公开(公告)日：2011-05-05
申请号：US13000786
申请日：2009-06-17
Applicant: Henrik Otto Stahl , Pat A. Han
Inventor： Henrik Otto Stahl , Pat A. Han
CPC classification number: C01C1/0405 , C01B3/025 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/52 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/068 , C01B2203/0811 , C01B2203/0844 , C01B2203/0894 , C01B2203/1241 , C01B2203/1258 , C01B2203/141 , C01C1/0452 , C01C1/0488 , F22B1/1838 , F28D7/0075 , F28D7/06 , F28F9/26 , Y02P20/129 , Y02P20/52
Abstract: Process for the production of ammonia from a hydrocarbon feedstock all steam produced in the waste heat boilers of the reforming and ammonia section of the plant is superheated in one or more steam superheaters located downstream the ammonia converter in the ammonia section of the plant. There is no need for steam superheater (s) in the reforming section of the plant to cool the synthesis gas. A steam superheater for use in the process is also provided. The superheater comprises two compartments in which the first and second compartments are connected in series with respect to the steam flow and in parallel with respect to the process gas flow.
Abstract translation: 用于从烃原料生产氨的方法在设备的氨部分中的氨转化器下游的一个或多个蒸汽过热器中过热在废气热锅炉中产生的所有蒸汽的重整和氨段的蒸汽过热。 在工厂的重整部分不需要蒸汽过热器来冷却合成气。 还提供了用于该过程的蒸汽过热器。 过热器包括两个室，其中第一和第二隔室相对于蒸汽流串联连接并且相对于处理气体流平行连接。
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