-
公开(公告)号:US08240370B2
公开(公告)日:2012-08-14
申请号:US12642249
申请日:2009-12-18
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/065 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/1247 , C01B2203/1258 , C01B2203/146 , C01B2203/86 , Y02P20/13 , Y02P30/30
摘要: Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam hydrocarbon reformer. Combustion product gas from the reformer is used to generate wet steam in a once-through steam generator from produced water recycled from the reservoir. The wet steam is used for the steam-assisted extraction of heavy hydrocarbons. The reformer has a heat exchanger section where a heat exchanger is suitable for processing the produced water by once-through steam generation and is suitable for mechanical cleaning.
摘要翻译: 用于生产氢气和蒸汽的重整器和方法,其中蒸汽用于蒸汽辅助提取重质烃。 将蒸汽注入含烃储存器中。 碳氢化合物与储存水一起从生产的水中提取出来。 在催化蒸汽烃重整器中产生氢。 来自重整器的燃烧产物气体用于在从储存器再循环的生产水中的直通蒸汽发生器中产生湿蒸汽。 湿蒸汽用于蒸汽辅助提取重质烃。 重整器具有热交换器部分,其中热交换器适于通过一次蒸汽产生来处理生产的水,并且适合于机械清洁。
-
公开(公告)号:US20110146991A1
公开(公告)日:2011-06-23
申请号:US12642249
申请日:2009-12-18
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/065 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/1247 , C01B2203/1258 , C01B2203/146 , C01B2203/86 , Y02P20/13 , Y02P30/30
摘要: Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam hydrocarbon reformer. Combustion product gas from the reformer is used to generate wet steam in a once-through steam generator from produced water recycled from the reservoir. The wet steam is used for the steam-assisted extraction of heavy hydrocarbons. The reformer has a heat exchanger section where a heat exchanger is suitable for processing the produced water by once-through steam generation and is suitable for mechanical cleaning.
摘要翻译: 用于生产氢气和蒸汽的重整器和方法,其中蒸汽用于蒸汽辅助提取重质烃。 将蒸汽注入含烃储存器中。 碳氢化合物与储存水一起从生产的水中提取出来。 在催化蒸汽烃重整器中产生氢。 来自重整器的燃烧产物气体用于在从储存器再循环的生产水中的直通蒸汽发生器中产生湿蒸汽。 湿蒸汽用于蒸汽辅助提取重质烃。 重整器具有热交换器部分,其中热交换器适于通过一次蒸汽产生来处理生产的水,并且适合于机械清洁。
-
公开(公告)号:US08414666B2
公开(公告)日:2013-04-09
申请号:US13547329
申请日:2012-07-12
IPC分类号: B01J7/00
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/065 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/1247 , C01B2203/1258 , C01B2203/146 , C01B2203/86 , Y02P20/13 , Y02P30/30
摘要: Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam hydrocarbon reformer. Combustion product gas from the reformer is used to generate wet steam in a once-through steam generator from produced water recycled from the reservoir. The wet steam is used for the steam-assisted extraction of heavy hydrocarbons. The reformer has a heat exchanger section including a first heat exchanger and a second heat exchanger downstream of the first heat exchanger. The second heat exchanger is suitable for processing the produced water by once-through steam generation and is suitable for mechanical cleaning. The reformer also has a first exhaust downstream of the second heat exchanger and a closeable second exhaust downstream of the first heat exchanger.
摘要翻译: 用于生产氢气和蒸汽的重整器和方法,其中蒸汽用于蒸汽辅助提取重质烃。 将蒸汽注入含烃储存器中。 碳氢化合物与储存水一起从生产的水中提取出来。 在催化蒸汽烃重整器中产生氢。 来自重整器的燃烧产物气体用于在从储存器再循环的生产水中的直通蒸汽发生器中产生湿蒸汽。 湿蒸汽用于蒸汽辅助提取重质烃。 重整器具有热交换器部分,其包括第一热交换器和在第一热交换器下游的第二热交换器。 第二个热交换器适用于通过一次蒸汽生成来处理生产的水,适用于机械清洗。 重整器还具有第二热交换器下游的第一排气和第一热交换器下游的可封闭的第二排气。
-
公开(公告)号:US20120294783A1
公开(公告)日:2012-11-22
申请号:US13547329
申请日:2012-07-12
IPC分类号: B01J7/00
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/065 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/1247 , C01B2203/1258 , C01B2203/146 , C01B2203/86 , Y02P20/13 , Y02P30/30
摘要: Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam hydrocarbon reformer. Combustion product gas from the reformer is used to generate wet steam in a once-through steam generator from produced water recycled from the reservoir. The wet steam is used for the steam-assisted extraction of heavy hydrocarbons. The reformer has a heat exchanger section where a heat exchanger is suitable for processing the produced water by once-through steam generation and is suitable for mechanical cleaning.
摘要翻译: 用于生产氢气和蒸汽的重整器和方法,其中蒸汽用于蒸汽辅助提取重质烃。 将蒸汽注入含烃储存器中。 碳氢化合物与储存水一起从生产的水中提取出来。 在催化蒸汽烃重整器中产生氢。 来自重整器的燃烧产物气体用于在从储存器再循环的生产水中的直通蒸汽发生器中产生湿蒸汽。 湿蒸汽用于蒸汽辅助提取重质烃。 重整器具有热交换器部分,其中热交换器适于通过一次蒸汽产生来处理生产的水,并且适合于机械清洁。
-
公开(公告)号:US20090232729A1
公开(公告)日:2009-09-17
申请号:US12101261
申请日:2008-04-11
申请人: Eugene S. Genkin , Stephen Paul DiMartino, SR. , Miguel Rafael Alvarez , David Anthony Zagnoli , Christopher Francis Harris
发明人: Eugene S. Genkin , Stephen Paul DiMartino, SR. , Miguel Rafael Alvarez , David Anthony Zagnoli , Christopher Francis Harris
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/043 , C01B2203/047 , C01B2203/048 , C01B2203/0495 , C01B2203/06 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/142 , C01B2203/146 , C01B2203/148 , C01B2203/84 , Y02P20/129
摘要: A method for generating hydrogen and/or synthesis gas in a production facility where little or no export steam is produced. Most or all of the high pressure steam produced from the waste heat from the process is used in the steam-hydrocarbon reformer with little or no steam export. The method uses oxygen enhanced combustion which may involve oxygen lancing and/or oxygen-enrichment. Plant efficiencies using the method and prior art-type methods are compared.
摘要翻译: 一种在生产设备中产生氢气和/或合成气的方法,其中产生很少或不产生出口蒸汽。 大部分或全部由该方法产生的废热产生的高压蒸汽用于蒸汽 - 烃重整器,其蒸汽输出很少或不产生。 该方法使用氧增强燃烧,其可以涉及氧气穿刺和/或氧气富集。 比较使用方法和现有技术类型方法的植物效率。
-
公开(公告)号:US07988948B2
公开(公告)日:2011-08-02
申请号:US12122160
申请日:2008-05-16
IPC分类号: C01B3/26
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0475 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/142 , C01B2203/148 , C01B2203/84 , Y02C10/08 , Y02P20/128 , Y02P20/129
摘要: A method for generating hydrogen and/or syngas in a production facility where little or no export steam is produced. Most or all of the steam produced from the waste heat from the process is used in the steam-hydrocarbon reformer. Reformed gas is passed to a pressure swing adsorption system for H2 purification. In the method, CO2 is removed from the pressure swing adsorber residual gas prior to recycling the residual gas to the reformer for use as feed and as fuel. Plant efficiencies using the method and prior art-type methods are compared.
摘要翻译: 一种在生产设备中产生氢气和/或合成气的方法,其中产生很少或不产生出口蒸汽。 大部分或全部由该方法的废热产生的蒸汽用于蒸汽 - 烃重整器。 改性气体通入变压吸附系统进行H2纯化。 在该方法中,在将残余气体再循环到重整器中用作进料和燃料之前,从变压吸附器残留气体中除去CO 2。 比较使用方法和现有技术类型方法的植物效率。
-
公开(公告)号:US07850944B2
公开(公告)日:2010-12-14
申请号:US12101261
申请日:2008-04-11
申请人: Eugene S. Genkin , Stephen Paul DiMartino, Sr. , Miguel Rafael Alvarez , David Anthony Zagnoli , Christopher Francis Harris
发明人: Eugene S. Genkin , Stephen Paul DiMartino, Sr. , Miguel Rafael Alvarez , David Anthony Zagnoli , Christopher Francis Harris
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/043 , C01B2203/047 , C01B2203/048 , C01B2203/0495 , C01B2203/06 , C01B2203/0816 , C01B2203/0827 , C01B2203/0883 , C01B2203/0894 , C01B2203/1058 , C01B2203/142 , C01B2203/146 , C01B2203/148 , C01B2203/84 , Y02P20/129
摘要: A method for generating hydrogen and/or synthesis gas in a production facility where little or no export steam is produced. Most or all of the high pressure steam produced from the waste heat from the process is used in the steam-hydrocarbon reformer with little or no steam export. The method uses oxygen enhanced combustion which may involve oxygen lancing and/or oxygen-enrichment. Plant efficiencies using the method and prior art-type methods are compared.
摘要翻译: 一种在生产设备中产生氢气和/或合成气的方法,其中产生很少或不产生出口蒸汽。 大部分或全部由该方法产生的废热产生的高压蒸汽用于蒸汽 - 烃重整器,其蒸汽输出很少或不产生。 该方法使用氧增强燃烧,其可以涉及氧气穿刺和/或氧气富集。 比较使用方法和现有技术类型方法的植物效率。
-
公开(公告)号:US20090230359A1
公开(公告)日:2009-09-17
申请号:US12122160
申请日:2008-05-16
IPC分类号: C01B3/26
CPC分类号: C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0475 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/142 , C01B2203/148 , C01B2203/84 , Y02C10/08 , Y02P20/128 , Y02P20/129
摘要: A method for generating hydrogen and/or syngas in a production facility where little or no export steam is produced. Most or all of the steam produced from the waste heat from the process is used in the steam-hydrocarbon reformer. Reformed gas is passed to a pressure swing adsorption system for H2 purification. In the method, CO2 is removed from the pressure swing adsorber residual gas prior to recycling the residual gas to the reformer for use as feed and as fuel. Plant efficiencies using the method and prior art-type methods are compared.
摘要翻译: 一种在生产设备中产生氢气和/或合成气的方法,其中产生很少或不产生出口蒸汽。 大部分或全部由该方法的废热产生的蒸汽用于蒸汽 - 烃重整器。 改性气体通入变压吸附系统进行H2纯化。 在该方法中,在将残余气体再循环到重整器中用作进料和燃料之前,从变压吸附器残留气体中除去CO 2。 比较使用方法和现有技术类型方法的植物效率。
-
公开(公告)号:US07837973B2
公开(公告)日:2010-11-23
申请号:US11745706
申请日:2007-05-08
申请人: Gregory David Snyder , Stephen Paul DiMartino, Sr. , David Anthony Zagnoli , James Joseph Stango
发明人: Gregory David Snyder , Stephen Paul DiMartino, Sr. , David Anthony Zagnoli , James Joseph Stango
IPC分类号: C01B3/24
CPC分类号: C10J3/00 , C01B3/16 , C01B3/36 , C01B3/384 , C01B3/48 , C01B3/52 , C01B3/56 , C01B2203/0233 , C01B2203/0255 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/141 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C10J3/82 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/1618 , C10K3/04 , Y02P20/128
摘要: A hydrogen production method that integrates a catalytic steam reformer and a gasifier. Hydrogen is generated in a catalytic steam reformer at a high production rate or design capacity. The catalytic steam reformer is then turned down to a fraction of design capacity while a gasifier produces the needed hydrogen. During the turned down state of the catalytic steam reformer, more of a hydrogen-containing stream formed from gasifier effluent is fed to the catalytic steam reformer as a feed thereby reducing the flow rate of feedstock required for the catalytic steam reformer in the turned down state. Optionally, hydrogen mixtures from the catalytic steam reformer and gasifier are fed to one or more adsorbers for hydrogen purification and adsorber effluent is fired as fuel in the steam reformer furnace to provide a majority of the heat needed for the reforming reaction.
摘要翻译: 一种集成催化蒸汽重整器和气化器的氢气生产方法。 在催化蒸汽重整器中以高生产率或设计能力产生氢气。 然后将催化蒸汽重整器降低到设计容量的一小部分,而气化器产生所需的氢气。 在催化蒸汽重整器的关闭状态期间,由气化器流出物形成的更多的含氢物流作为进料被供给到催化蒸汽重整器,由此降低催化蒸汽重整器在向下状态下所需的原料流速 。 任选地,来自催化蒸汽重整器和气化器的氢混合物被供给到一个或多个吸附器进行氢气净化,并且将吸附器流出物作为燃料在蒸汽重整炉中燃烧以提供重整反应所需的大部分热量。
-
公开(公告)号:US20080279763A1
公开(公告)日:2008-11-13
申请号:US11745706
申请日:2007-05-08
申请人: Gregory David Snyder , Stephen Paul DiMartino, SR. , David Anthony Zagnoli , James Joseph Stango
发明人: Gregory David Snyder , Stephen Paul DiMartino, SR. , David Anthony Zagnoli , James Joseph Stango
IPC分类号: C01B3/02
CPC分类号: C10J3/00 , C01B3/16 , C01B3/36 , C01B3/384 , C01B3/48 , C01B3/52 , C01B3/56 , C01B2203/0233 , C01B2203/0255 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/141 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C10J3/82 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/1618 , C10K3/04 , Y02P20/128
摘要: A hydrogen production method that integrates a catalytic steam reformer and a gasifier. Hydrogen is generated in a catalytic steam reformer at a high production rate or design capacity. The catalytic steam reformer is then turned down to a fraction of design capacity while a gasifier produces the needed hydrogen. During the turned down state of the catalytic steam reformer, more of a hydrogen-containing stream formed from gasifier effluent is fed to the catalytic steam reformer as a feed thereby reducing the flow rate of feedstock required for the catalytic steam reformer in the turned down state. Optionally, hydrogen mixtures from the catalytic steam reformer and gasifier are fed to one or more adsorbers for hydrogen purification and adsorber effluent is fired as fuel in the steam reformer furnace to provide a majority of the heat needed for the reforming reaction.
摘要翻译: 一种集成催化蒸汽重整器和气化器的氢气生产方法。 在催化蒸汽重整器中以高生产率或设计能力产生氢气。 然后将催化蒸汽重整器降低到设计容量的一小部分,而气化器产生所需的氢气。 在催化蒸汽重整器的关闭状态期间,由气化器流出物形成的更多的含氢物流作为进料被供给到催化蒸汽重整器,由此降低催化蒸汽重整器在向下状态下所需的原料流速 。 任选地,来自催化蒸汽重整器和气化器的氢混合物被供给到一个或多个吸附器进行氢气净化,并且将吸附器流出物作为燃料在蒸汽重整炉中燃烧以提供重整反应所需的大部分热量。
-
-
-
-
-
-
-
-
-