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1.发明申请MULTI-ZONE REFORMING METHODS AND APPARATUS FOR CONVERSION OF DEVOLATILIZED BIOMASS TO SYNGAS 审中-公开多区域改造方法和将生物质转化为SYNGAS的装置公开(公告)号：US20110150722A1
公开(公告)日：2011-06-23
申请号：US13038739
申请日：2011-03-02
IPC分类号： B01J8/00
CPC分类号： C01B3/38 , C01B2203/0233 , C01B2203/04 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/1241 , C07C29/1516 , C10J3/485 , C10J2300/0976 , C10J2300/1853 , C10K1/026 , C10K3/006 , Y02E50/18 , Y02E50/32 , Y02P20/145 , C07C31/08
摘要： The present invention provides improved methods and apparatus for producing syngas from any carbon-containing feed material. In one aspect, a multi-zone reformer system is provided. A first reaction zone can reduce the presence of refractory tars, while a second reaction zone in communication with the first reaction zone can steam-reform methane and other components from the first reaction zone, to generate high-quality syngas suitable for conversion to liquid fuels, such as ethanol. Other embodiments employ a plurality of reaction zones for added system functionality.
摘要翻译： 本发明提供用于从任何含碳原料生产合成气的改进方法和装置。 一方面，提供了一种多区域重整器系统。 第一反应区可以减少耐火焦油的存在，而与第一反应区连通的第二反应区可以从第一反应区蒸汽重整甲烷和其它组分，以产生适合转化为液体燃料的高品质合成气 ，如乙醇。 其他实施例采用多个反应区用于附加的系统功能。
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公开(公告)号：US20090018371A1
公开(公告)日：2009-01-15
申请号：US12166203
申请日：2008-07-01
IPC分类号： C07C29/32
摘要： Methods and apparatus for producing alcohols from syngas are disclosed herein. In some variations, syngas is catalytically converted to methanol in a first reaction zone, and residual syngas from the first reaction zone is then catalytically converted to ethanol in a second reaction zone. Also, in some variations, syngas is catalytically converted to methanol in high yield in a first reaction zone, and the methanol is then converted (optionally, with additional syngas) to ethanol in a second reaction zone.
摘要翻译： 本文公开了从合成气生产醇的方法和装置。 在一些变化中，在第一反应区中将合成气催化转化成甲醇，然后在第二反应区将来自第一反应区的剩余合成气催化转化为乙醇。 而且，在一些变型中，合成气在第一反应区中以高产率被催化转化成甲醇，然后在第二反应区中将甲醇转化（任选地，与另外的合成气一起）转化为乙醇。
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3.发明授权Systems and methods for biomass gasifier reactor and receiver configuration 有权生物质气化炉反应器和接收器配置的系统和方法公开(公告)号：US08821599B2
公开(公告)日：2014-09-02
申请号：US12795910
申请日：2010-06-08
申请人： Christopher Perkins , Zoran Jovanovic , Steven Strand , Donna Kelley , Andrew Minden , Richard Ridley
发明人： Christopher Perkins , Zoran Jovanovic , Steven Strand , Donna Kelley , Andrew Minden , Richard Ridley
IPC分类号： B01J7/00
CPC分类号： C01B3/384 , B01J19/0013 , B01J19/0033 , B01J19/2445 , B01J19/245 , B01J2219/00117 , B01J2219/00186 , C01B3/22 , C01B3/34 , C01B2203/0216 , C01B2203/0233 , C01B2203/061 , C01B2203/0811 , C01B2203/1241 , C01B2203/1685 , C01B2203/84 , C07C29/15 , C07C29/1518 , C10G2/30 , C10G2/32 , C10G3/00 , C10G2300/1014 , C10G2300/1025 , C10G2300/807 , C10J3/00 , C10J3/466 , C10J3/482 , C10J3/485 , C10J3/506 , C10J3/54 , C10J3/56 , C10J3/58 , C10J3/60 , C10J3/62 , C10J3/721 , C10J3/723 , C10J3/82 , C10J3/84 , C10J2200/09 , C10J2200/15 , C10J2200/158 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/094 , C10J2300/0973 , C10J2300/0976 , C10J2300/0989 , C10J2300/0993 , C10J2300/1223 , C10J2300/123 , C10J2300/1284 , C10J2300/1292 , C10J2300/1621 , C10J2300/1659 , C10J2300/1665 , C10J2300/1693 , C10J2300/1853 , C10J2300/1861 , C10K1/024 , C10L1/04 , C10L2200/0492 , C10L2290/02 , C10L2290/04 , C10L2290/06 , C10L2290/08 , C10L2290/28 , C10L2290/42 , C10L2290/50 , C10L2290/52 , C10L2290/547 , F24S20/20 , Y02B40/18 , Y02E10/41 , Y02E50/18 , Y02E50/32 , Y02P20/129 , Y02P20/134 , Y02P20/136 , Y02P20/145 , Y02P30/20 , Y02T50/678 , C07C31/04
摘要： A method, apparatus, and system for solar-driven chemical plant may include a solar thermal receiver to absorb concentrated solar energy from an array of heliostats. Additionally, some embodiments may include a solar driven chemical reactor that has multiple reactor tubes. The concentrated solar energy drives the endothermic gasification reaction of the particles of biomass flowing through the reactor tubes. Some embodiments may also include an on-site fuel synthesis reactor that is geographically located on the same site as the chemical reactor and integrated to receive the hydrogen and carbon monoxide products from the gasification reaction.
摘要翻译： 用于太阳能驱动化学工厂的方法，装置和系统可以包括太阳能热接收器，以从日光反射阵列吸收集中的太阳能。 另外，一些实施例可以包括具有多个反应器管的太阳能驱动的化学反应器。 集中的太阳能驱动流过反应器管的生物质颗粒的吸热气化反应。 一些实施方案还可以包括地理位置位于与化学反应器相同的位置上的现场燃料合成反应器，并且被整合以从气化反应接收氢气和一氧化碳产物。
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4.发明授权Multi-zone reforming methods and apparatus for conversion of devolatilized biomass to syngas 失效用于将脱挥发分生物质转化为合成气的多区域重整方法和装置公开(公告)号：US07919070B2
公开(公告)日：2011-04-05
申请号：US12628409
申请日：2009-12-01
CPC分类号： C01B3/38 , C01B2203/0233 , C01B2203/04 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/1241 , C07C29/1516 , C10J3/485 , C10J2300/0976 , C10J2300/1853 , C10K1/026 , C10K3/006 , Y02E50/18 , Y02E50/32 , Y02P20/145 , C07C31/08
摘要： The present invention provides improved methods and apparatus for producing syngas from any carbon-containing feed material. In one aspect, a multi-zone reformer system is provided. A first reaction zone can reduce the presence of refractory tars, while a second reaction zone in communication with the first reaction zone can steam-reform methane and other components from the first reaction zone, to generate high-quality syngas suitable for conversion to liquid fuels, such as ethanol. Other embodiments employ a plurality of reaction zones for added system functionality.
摘要翻译： 本发明提供用于从任何含碳原料生产合成气的改进方法和装置。 一方面，提供了一种多区域重整器系统。 第一反应区可以减少耐火焦油的存在，而与第一反应区连通的第二反应区可以从第一反应区蒸汽重整甲烷和其它组分，以产生适合转化为液体燃料的高品质合成气 ，如乙醇。 其他实施例采用多个反应区用于附加的系统功能。
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5.发明申请SYSTEMS AND METHODS FOR BIOMASS GASIFIER REACTOR AND RECEIVER CONFIGURATION 有权生物质气化器反应器和接收器配置的系统和方法公开(公告)号：US20100247387A1
公开(公告)日：2010-09-30
申请号：US12795910
申请日：2010-06-08
申请人： Christopher Perkins , Zoran Jovanovic , Steven Strand , Donna Kelley , Andrew Minden , Richard Ridley
发明人： Christopher Perkins , Zoran Jovanovic , Steven Strand , Donna Kelley , Andrew Minden , Richard Ridley
CPC分类号： C01B3/384 , B01J19/0013 , B01J19/0033 , B01J19/2445 , B01J19/245 , B01J2219/00117 , B01J2219/00186 , C01B3/22 , C01B3/34 , C01B2203/0216 , C01B2203/0233 , C01B2203/061 , C01B2203/0811 , C01B2203/1241 , C01B2203/1685 , C01B2203/84 , C07C29/15 , C07C29/1518 , C10G2/30 , C10G2/32 , C10G3/00 , C10G2300/1014 , C10G2300/1025 , C10G2300/807 , C10J3/00 , C10J3/466 , C10J3/482 , C10J3/485 , C10J3/506 , C10J3/54 , C10J3/56 , C10J3/58 , C10J3/60 , C10J3/62 , C10J3/721 , C10J3/723 , C10J3/82 , C10J3/84 , C10J2200/09 , C10J2200/15 , C10J2200/158 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/094 , C10J2300/0973 , C10J2300/0976 , C10J2300/0989 , C10J2300/0993 , C10J2300/1223 , C10J2300/123 , C10J2300/1284 , C10J2300/1292 , C10J2300/1621 , C10J2300/1659 , C10J2300/1665 , C10J2300/1693 , C10J2300/1853 , C10J2300/1861 , C10K1/024 , C10L1/04 , C10L2200/0492 , C10L2290/02 , C10L2290/04 , C10L2290/06 , C10L2290/08 , C10L2290/28 , C10L2290/42 , C10L2290/50 , C10L2290/52 , C10L2290/547 , F24S20/20 , Y02B40/18 , Y02E10/41 , Y02E50/18 , Y02E50/32 , Y02P20/129 , Y02P20/134 , Y02P20/136 , Y02P20/145 , Y02P30/20 , Y02T50/678 , C07C31/04
摘要： A method, apparatus, and system for solar-driven chemical plant may include a solar thermal receiver to absorb concentrated solar energy from an array of heliostats. Additionally, some embodiments may include a solar driven chemical reactor that has multiple reactor tubes. The concentrated solar energy drives the endothermic gasification reaction of the particles of biomass flowing through the reactor tubes. Some embodiments may also include an on-site fuel synthesis reactor that is geographically located on the same site as the chemical reactor and integrated to receive the hydrogen and carbon monoxide products from the gasification reaction.
摘要翻译： 用于太阳能驱动化学工厂的方法，装置和系统可以包括太阳能热接收器，以从日光反射阵列吸收集中的太阳能。 另外，一些实施例可以包括具有多个反应器管的太阳能驱动的化学反应器。 集中的太阳能驱动流过反应器管的生物质颗粒的吸热气化反应。 一些实施方案还可以包括地理位置位于与化学反应器相同的位置上的现场燃料合成反应器，并且被整合以从气化反应接收氢气和一氧化碳产物。
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公开(公告)号：US20100242354A1
公开(公告)日：2010-09-30
申请号：US12796471
申请日：2010-06-08
申请人： Christopher Perkins , Zoran Jovanovic , Courtland Hilton , Brittany Lancaster , Andrew Minden , Richard Ridley , Donna Kelley
发明人： Christopher Perkins , Zoran Jovanovic , Courtland Hilton , Brittany Lancaster , Andrew Minden , Richard Ridley , Donna Kelley
CPC分类号： C01B3/384 , B01J19/0013 , B01J19/0033 , B01J19/2445 , B01J19/245 , B01J2219/00117 , B01J2219/00186 , C01B3/22 , C01B3/34 , C01B2203/0216 , C01B2203/0233 , C01B2203/061 , C01B2203/0811 , C01B2203/1241 , C01B2203/1685 , C01B2203/84 , C07C29/15 , C07C29/1518 , C10G2/30 , C10G2/32 , C10G3/00 , C10G2300/1014 , C10G2300/1025 , C10G2300/807 , C10J3/00 , C10J3/466 , C10J3/482 , C10J3/485 , C10J3/506 , C10J3/54 , C10J3/56 , C10J3/58 , C10J3/60 , C10J3/62 , C10J3/721 , C10J3/723 , C10J3/82 , C10J3/84 , C10J2200/09 , C10J2200/15 , C10J2200/158 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/094 , C10J2300/0973 , C10J2300/0976 , C10J2300/0989 , C10J2300/0993 , C10J2300/1223 , C10J2300/123 , C10J2300/1284 , C10J2300/1292 , C10J2300/1621 , C10J2300/1659 , C10J2300/1665 , C10J2300/1693 , C10J2300/1853 , C10J2300/1861 , C10K1/024 , C10L1/04 , C10L2200/0492 , C10L2290/02 , C10L2290/04 , C10L2290/06 , C10L2290/08 , C10L2290/28 , C10L2290/42 , C10L2290/50 , C10L2290/52 , C10L2290/547 , F24S20/20 , Y02B40/18 , Y02E10/41 , Y02E50/18 , Y02E50/32 , Y02P20/129 , Y02P20/134 , Y02P20/136 , Y02P20/145 , Y02P30/20 , Y02T50/678 , C07C31/04
摘要： A method, apparatus, and system for a solar-driven chemical plant that manages variations in solar energy are disclosed. Some embodiments include a solar thermal receiver to absorb concentrated solar energy, a solar driven chemical reactor contained within the solar thermal receiver, and an entrained gas biomass feed system that uses an entrainment carrier gas and supplies a variety of biomass sources fed as particles into the solar driven chemical reactor. Inner walls of the solar thermal receiver and the chemical reactor can be made from materials selected to transfer energy. Some embodiments include a control system that may be configured to balance the gasification reaction of biomass particles with the available concentrated solar energy and additional variable parameters including, but not limited to, a fixed range of particle sizes, temperature of the chemical reactor, and residence time of the particles in a reaction zone in the chemical reactor.
摘要翻译： 公开了一种管理太阳能变化的太阳能驱动化学工厂的方法，装置和系统。 一些实施例包括用于吸收集中的太阳能的太阳能热接收器，包含在太阳能热接收器内的太阳能驱动的化学反应器，以及夹带的气体生物质进料系统，其使用夹带载气并将各种作为颗粒进料的生物质源供应到 太阳能驱动化学反应堆。 太阳能热接收器和化学反应器的内壁可以由选择用于传递能量的材料制成。 一些实施方案包括控制系统，其可被配置为平衡生物质颗粒的气化反应与可利用的集中的太阳能和附加的可变参数，包括但不限于固定范围的粒度，化学反应器的温度和居住 颗粒在化学反应器的反应区中的时间。
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7.发明申请MULTI-ZONE REFORMING METHODS AND APPARATUS FOR CONVERSION OF DEVOLATILIZED BIOMASS TO SYNGAS 失效多区域改造方法和将生物质转化为SYNGAS的装置公开(公告)号：US20100137459A1
公开(公告)日：2010-06-03
申请号：US12628409
申请日：2009-12-01
CPC分类号： C01B3/38 , C01B2203/0233 , C01B2203/04 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/1241 , C07C29/1516 , C10J3/485 , C10J2300/0976 , C10J2300/1853 , C10K1/026 , C10K3/006 , Y02E50/18 , Y02E50/32 , Y02P20/145 , C07C31/08
摘要： The present invention provides improved methods and apparatus for producing syngas from any carbon-containing feed material. In one aspect, a multi-zone reformer system is provided. A first reaction zone can reduce the presence of refractory tars, while a second reaction zone in communication with the first reaction zone can steam-reform methane and other components from the first reaction zone, to generate high-quality syngas suitable for conversion to liquid fuels, such as ethanol. Other embodiments employ a plurality of reaction zones for added system functionality.
摘要翻译： 本发明提供用于从任何含碳原料生产合成气的改进方法和装置。 一方面，提供了一种多区域重整器系统。 第一反应区可以减少耐火焦油的存在，而与第一反应区连通的第二反应区可以从第一反应区蒸汽重整甲烷和其它组分，以产生适合转化为液体燃料的高品质合成气 ，如乙醇。 其他实施例采用多个反应区用于附加的系统功能。
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