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    Process for the Preparation and Conversion of Synthesis Gas.
    11.
    发明申请
    Process for the Preparation and Conversion of Synthesis Gas. 有权
    合成气的制备和转化方法。

    公开(公告)号：US20090186952A1

    公开(公告)日：2009-07-23

    申请号：US11922380

    申请日：2006-06-14

    申请人： Andre Peter Steynberg ,  Ib Dybkjaer ,  Kim Aasberg-Petersen

    发明人： Andre Peter Steynberg ,  Ib Dybkjaer ,  Kim Aasberg-Petersen

    IPC分类号： C07C27/00

    CPC分类号： C01B3/384 ,  B01J23/755 ,  B01J37/0201 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/0238 ,  C01B2203/0244 ,  C01B2203/062 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/127 ,  C10G2/32 ,  C10G2/332 ,  C10G2300/4081 ,  C10K1/005 ,  C10K3/006 ,  Y02P20/52

    摘要： A process (10) for the preparation and conversion of synthesis gas includes reforming a feed gas (34) comprising methane in a reforming stage (18) to produce synthesis gas (46) which includes hydrogen and carbon monoxide. Some of the hydrogen and carbon monoxide is converted to a Fischer-Tropsch product (48) in a Fischer-Tropsch hydrocarbon synthesis stage (24). A tail gas (52), including unreacted hydrogen and carbon monoxide, methane and carbon dioxide, is separated from the Fischer-Tropsch product (48). In a tail gas treatment stage (28,30), the tail gas (52) is treated by reforming the methane in the tail gas (52) with steam (66) and removing carbon dioxide to produce a hydrogen rich gas (56). The tail gas treatment stage (28,30) may be either a combined tail gas treatment stage (28,30) or a composite tail gas treatment stage. The carbon dioxide from the tail gas treatment stage (28,30) is fed to the reforming stage (18).

    摘要翻译： 用于制备和转化合成气的方法（10）包括在重整阶段（18）中重整包含甲烷的进料气体（34）以产生包括氢气和一氧化碳的合成气体（46）。 在费 - 托烃合成阶段（24）中，一些氢和一氧化碳转化成费 - 托产物（48）。 包含未反应的氢气和一氧化碳的甲烷和二氧化碳的尾气（52）从费 - 托产物（48）中分离出来。 在尾气处理阶段（28,30）中，通过用蒸汽（66）重整尾气（52）中的甲烷并除去二氧化碳以产生富氢气体（56）来处理尾气（52）。 尾气处理阶段（28,30）可以是组合尾气处理阶段（28,30）或复合尾气处理阶段。 来自尾气处理阶段（28,30）的二氧化碳被供给到重整阶段（18）。

    Production of hydrogen and carbon monoxide containing synthesis gas by partial oxidation
    12.
    发明授权
    Production of hydrogen and carbon monoxide containing synthesis gas by partial oxidation 失效
    通过部分氧化生产含氢和一氧化碳的合成气

    公开(公告)号：US06730285B2

    公开(公告)日：2004-05-04

    申请号：US09955455

    申请日：2001-09-18

    申请人： Kim Aasberg-Petersen ,  Thomas Sandahl Christensen

    发明人： Kim Aasberg-Petersen ,  Thomas Sandahl Christensen

    IPC分类号： C01B326

    CPC分类号： C01B3/382 ,  C01B3/386 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0844 ,  C01B2203/1241 ,  C01B2203/143 ,  C01B2203/82

    摘要： A process for the preparation of a synthesis gas containing hydrogen and carbon monoxide by a combination of catalytic partial oxidation and further an autothermal reforming process, comprising (a) providing separate streams of predetermined proportions of a hydrocarbon feedstock, an oxygen source and of process steam, (b) injecting said separate streams into a catalytic partial oxidation reaction zone to react, and to form a prereformed product stream, (c) introducing the prereformed product and a predetermined proportion of a second oxygen source into a further partial oxidation process step forming a further partially oxidised process stream by flame reactions, (d) reacting the further partially oxidised process stream in the reaction zone constituting a steam reforming process step to form a synthesis gas product stream, and (e) withdrawing the synthesis gas product stream from the further partial oxidation process step and the steam reforming process step, the two steps constituting the autothermal reforming process.

    摘要翻译： 一种通过催化部分氧化和进一步的自热重整方法的组合制备含有氢和一氧化碳的合成气的方法，包括（a）提供预定比例的烃原料，氧源和工艺蒸汽的单独流 ，（b）将所述分离的物流注入催化部分氧化反应区以进行反应，并形成预重整的产物流，（c）将预转化产物和预定比例的第二氧源引入另外的部分氧化工艺步骤中形成 通过火焰反应进一步部分氧化的工艺流，（d）使构成蒸汽重整工艺步骤的反应区中的进一步部分氧化的工艺流反应以形成合成气产物流，和（e）从合成气产物流中取出合成气产物流 进一步的部分氧化工艺步骤和蒸汽重整工艺步骤，两步构成 e自热重整过程。

    Process for the preparation and conversion of synthesis gas
    14.
    发明授权
    Process for the preparation and conversion of synthesis gas 有权
    合成气的制备和转化方法

    公开(公告)号：US08106102B2

    公开(公告)日：2012-01-31

    申请号：US11922380

    申请日：2006-06-14

    申请人： Andre Peter Steynberg ,  Ib Dybkjaer ,  Kim Aasberg-Petersen

    发明人： Andre Peter Steynberg ,  Ib Dybkjaer ,  Kim Aasberg-Petersen

    IPC分类号： C07C27/00

    CPC分类号： C01B3/384 ,  B01J23/755 ,  B01J37/0201 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/0238 ,  C01B2203/0244 ,  C01B2203/062 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/127 ,  C10G2/32 ,  C10G2/332 ,  C10G2300/4081 ,  C10K1/005 ,  C10K3/006 ,  Y02P20/52

    摘要： A process (10) for the preparation and conversion of synthesis gas includes reforming a feed gas (34) comprising methane in a reforming stage (18) to produce synthesis gas (46) which includes hydrogen and carbon monoxide. Some of the hydrogen and carbon monoxide is converted to a Fischer-Tropsch product (48) in a Fischer-Tropsch hydrocarbon synthesis stage (24). A tail gas (52), including unreacted hydrogen and carbon monoxide, methane and carbon dioxide, is separated from the Fischer-Tropsch product (48). In a tail gas treatment stage (28,30), the tail gas (52) is treated by reforming the methane in the tail gas (52) with steam (66) and removing carbon dioxide to produce a hydrogen rich gas (56). The tail gas treatment stage (28,30) may be either a combined tail gas treatment stage (28,30) or a composite tail gas treatment stage. The carbon dioxide from the tail gas treatment stage (28,30) is fed to the reforming stage (18).

    摘要翻译： 用于制备和转化合成气的方法（10）包括在重整阶段（18）中重整包含甲烷的进料气体（34）以产生包括氢气和一氧化碳的合成气体（46）。 在费 - 托烃合成阶段（24）中，一些氢和一氧化碳转化成费 - 托产物（48）。 包含未反应的氢气和一氧化碳的甲烷和二氧化碳的尾气（52）从费 - 托产物（48）中分离出来。 在尾气处理阶段（28,30）中，通过用蒸汽（66）重整尾气（52）中的甲烷并除去二氧化碳以产生富氢气体（56）来处理尾气（52）。 尾气处理阶段（28,30）可以是组合尾气处理阶段（28,30）或复合尾气处理阶段。 来自尾气处理阶段（28,30）的二氧化碳被供给到重整阶段（18）。

    Process for reforming ethanol
    15.
    发明申请
    Process for reforming ethanol 有权
    乙醇改性方法

    公开(公告)号：US20060057058A1

    公开(公告)日：2006-03-16

    申请号：US10940762

    申请日：2004-09-15

    申请人： Soren Dahl ,  Charlotte Nielsen ,  Poul Erik Nielsen ,  Kim Aasberg-Petersen

    发明人： Soren Dahl ,  Charlotte Nielsen ,  Poul Erik Nielsen ,  Kim Aasberg-Petersen

    IPC分类号： C01B3/02

    CPC分类号： C01B3/382 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/1241 ,  C01B2203/1264 ,  C01B2203/142

    摘要： Process for selectively reforming ethanol to a hydrogen-rich product in the presence of at least one catalyst comprising a catalytically active material supported on a carrier, the process comprising the following steps in which the at least one catalyst is active: transferring a stream of ethanol and steam and a hydrogen-comprising stream, the molar ratio of ethanol to hydrogen being 0.2-1, to a dehydration/hydrogenation reactor for dehydrating ethanol to ethylene and for hydrogenating ethylene to produce an ethane-containing stream, adiabatically pre-reforming the ethane-comprising stream to a stream comprising methane, steam reforming the stream comprising methane to produce a mixture comprising hydrogen and carbon monoxide, converting the mixture comprising hydrogen and carbon monoxide from the steam reforming step under water gas shift conditions to produce a hydrogen-rich product stream.

    摘要翻译： 在至少一种包含负载在载体上的催化活性物质的催化剂存在下，将乙醇选择性地重整成富氢产物的方法，所述方法包括以下步骤：其中所述至少一种催化剂是有活性的：将乙醇流 和蒸汽和含氢气流，乙醇与氢气的摩尔比为0.2-1，用于脱乙醇/氢化反应器，用于将乙醇脱水成乙烯和氢化乙烯以产生含乙烷的流，绝热地重整乙烷 包含甲烷的流，对包含甲烷的流进行蒸汽重整以产生包含氢气和一氧化碳的混合物，在水煤气变换条件下将来自蒸汽重整步骤的氢和一氧化碳的混合物转化，以产生富氢产物 流。

    Process for reforming ethanol to hydrogen-rich products
    20.
    发明授权
    Process for reforming ethanol to hydrogen-rich products 有权
    将乙醇重整成富氢产品的方法

    公开(公告)号：US07585339B2

    公开(公告)日：2009-09-08

    申请号：US10940762

    申请日：2004-09-15

    申请人： Søren Dahl ,  Charlotte Stub Nielsen ,  Poul Erik Højlund Nielsen ,  Kim Aasberg-Petersen

    发明人： Søren Dahl ,  Charlotte Stub Nielsen ,  Poul Erik Højlund Nielsen ,  Kim Aasberg-Petersen

    IPC分类号： C01B3/02

    CPC分类号： C01B3/382 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/1241 ,  C01B2203/1264 ,  C01B2203/142

    摘要： Process for selectively reforming ethanol to a hydrogen-rich product in the presence of at least one catalyst comprising a catalytically active material supported on a carrier, the process comprising the following steps in which the at least one catalyst is active: transferring a stream of ethanol and steam and a hydrogen-comprising stream, the molar ratio of ethanol to hydrogen being 0.2-1, to a dehydration/hydrogenation reactor for dehydrating ethanol to ethylene and for hydrogenating ethylene to produce an ethane-containing stream, adiabatically pre-reforming the ethane-comprising stream to a stream comprising methane, steam reforming the stream comprising methane to produce a mixture comprising hydrogen and carbon monoxide, converting the mixture comprising hydrogen and carbon monoxide from the steam reforming step under water gas shift conditions to produce a hydrogen-rich product stream.

    摘要翻译： 在至少一种包含负载在载体上的催化活性物质的催化剂存在下，将乙醇选择性地重整成富氢产物的方法，所述方法包括以下步骤：其中所述至少一种催化剂是有活性的：将乙醇流 和蒸汽和含氢气流，乙醇与氢气的摩尔比为0.2-1，用于脱乙醇/氢化反应器，用于将乙醇脱水成乙烯和氢化乙烯以产生含乙烷的流，绝热地重整乙烷 包含甲烷的流，对包含甲烷的流进行蒸汽重整以产生包含氢气和一氧化碳的混合物，在水煤气变换条件下将来自蒸汽重整步骤的氢和一氧化碳的混合物转化，以产生富氢产物 流。