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公开(公告)号：US20100243961A1
公开(公告)日：2010-09-30
申请号：US12796319
申请日：2010-06-08
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 are disclosed. An embodiment may include a solar thermal receiver aligned to absorb concentrated solar energy from one or more solar energy concentrating fields. A solar driven chemical reactor may include multiple reactor tubes located inside the solar thermal receiver. The multiple reactor tubes can be used to gasify particles of biomass in the presence of a carrier gas. The gasification reaction may produce reaction products that include hydrogen and carbon monoxide gas having an exit temperature from the tubes exceeding 1000 degrees C. An embodiment can include a quench zone immediately downstream of an exit of the chemical reactor. The quench zone may immediately quench via rapid cooling of at least the hydrogen and carbon monoxide reaction products within 0.1-10 seconds of exiting the chemical reactor to a temperature of 800 degrees C. or less.
摘要翻译： 公开了一种用于太阳能驱动的化学设备的方法，装置和系统。 一个实施例可以包括对准以从一个或多个太阳能集中场吸收集中的太阳能的太阳能热接收器。 太阳能驱动的化学反应器可以包括位于太阳能热接收器内部的多个反应器管。 多个反应器管可用于在存在载气的情况下气化生物质颗粒。 气化反应可以产生包括氢气和一氧化碳气体的反应产物，其具有超过1000℃的管的出口温度。实施方案可以包括紧邻化学反应器出口下游的骤冷区。 骤冷区可以在离开化学反应器的0.1-10秒内通过至少一种氢氧化物和一氧化碳反应产物的快速冷却立即淬灭至800摄氏度或更低的温度。
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公开(公告)号：US08709112B2
公开(公告)日：2014-04-29
申请号：US12796319
申请日：2010-06-08
IPC分类号： C10J3/08
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 are disclosed. An embodiment may include a solar thermal receiver aligned to absorb concentrated solar energy from one or more solar energy concentrating fields. A solar driven chemical reactor may include multiple reactor tubes located inside the solar thermal receiver. The multiple reactor tubes can be used to gasify particles of biomass in the presence of a carrier gas. The gasification reaction may produce reaction products that include hydrogen and carbon monoxide gas having an exit temperature from the tubes exceeding 1000 degrees C. An embodiment can include a quench zone immediately downstream of an exit of the chemical reactor. The quench zone may immediately quench via rapid cooling of at least the hydrogen and carbon monoxide reaction products within 0.1-10 seconds of exiting the chemical reactor to a temperature of 800 degrees C. or less.
摘要翻译： 公开了一种用于太阳能驱动的化学设备的方法，装置和系统。 一个实施例可以包括对准以从一个或多个太阳能集中场吸收集中的太阳能的太阳能热接收器。 太阳能驱动的化学反应器可以包括位于太阳能热接收器内部的多个反应器管。 多个反应器管可用于在存在载气的情况下气化生物质颗粒。 气化反应可以产生包括氢气和一氧化碳气体的反应产物，其具有超过1000℃的管的出口温度。实施方案可以包括紧邻化学反应器出口下游的骤冷区。 骤冷区可以在离开化学反应器的0.1-10秒内通过至少一种氢氧化物和一氧化碳反应产物的快速冷却立即淬灭至800摄氏度或更低的温度。
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公开(公告)号：US20100242353A1
公开(公告)日：2010-09-30
申请号：US12796222
申请日：2010-06-08
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 bio-refinery that may include a entrained-flow biomass feed system that is feedstock flexible via particle size control of the biomass. Some embodiments include a chemical reactor that receives concentrated solar thermal energy from an array of heliostats. The entrained-flow biomass feed system can use an entrainment carrier gas and supplies a variety of biomass sources fed as particles into the solar-driven chemical reactor. Biomass sources in a raw state or partially torrified state may be used, as long as parameters such as particle size of the biomass are controlled. Additionally, concentrated solar thermal energy can drive gasification of the particles. An on-site fuel synthesis reactor may receive the hydrogen and carbon monoxide products from the gasification reaction use the hydrogen and carbon monoxide products in a hydrocarbon fuel synthesis process to create a liquid hydrocarbon fuel.
摘要翻译： 一种用于太阳能驱动的生物炼油厂的方法，装置和系统，其可以包括通过生物量的粒度控制而原料柔性的夹带流生物质进料系统。 一些实施例包括从定日镜阵列接收集中的太阳能热能的化学反应器。 夹带流生物质进料系统可以使用夹带载气，并将多种作为颗粒进料的生物质源供应到太阳能驱动的化学反应器中。 只要能够控制诸如生物质的粒度的参数，就可以使用处于原始状态或部分受束缚状态的生物质源。 此外，集中的太阳能热能可以驱动颗粒的气化。 现场燃料合成反应器可以从气化反应中接收氢气和一氧化碳产物，在烃燃料合成过程中使用氢气和一氧化碳产物以产生液态烃燃料。
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公开(公告)号：US09150803B2
公开(公告)日：2015-10-06
申请号：US12796222
申请日：2010-06-08
IPC分类号： C10J3/54 , C01B3/22 , C01B3/34 , C07C29/15 , C10J3/00 , C10G2/00 , C10J3/48 , C10J3/72 , F24J2/07 , C10J3/56
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 bio-refinery that may include a entrained-flow biomass feed system that is feedstock flexible via particle size control of the biomass. Some embodiments include a chemical reactor that receives concentrated solar thermal energy from an array of heliostats. The entrained-flow biomass feed system can use an entrainment carrier gas and supplies a variety of biomass sources fed as particles into the solar-driven chemical reactor. Biomass sources in a raw state or partially torrified state may be used, as long as parameters such as particle size of the biomass are controlled. Additionally, concentrated solar thermal energy can drive gasification of the particles. An on-site fuel synthesis reactor may receive the hydrogen and carbon monoxide products from the gasification reaction use the hydrogen and carbon monoxide products in a hydrocarbon fuel synthesis process to create a liquid hydrocarbon fuel.
摘要翻译： 一种用于太阳能驱动的生物炼油厂的方法，装置和系统，其可以包括通过生物量的粒度控制而原料柔性的夹带流生物质进料系统。 一些实施例包括从定日镜阵列接收集中的太阳能热能的化学反应器。 夹带流生物质进料系统可以使用夹带载气，并将多种作为颗粒进料的生物质源供应到太阳能驱动的化学反应器中。 只要能够控制诸如生物质的粒度的参数，就可以使用处于原始状态或部分受束缚状态的生物质源。 此外，集中的太阳能热能可以驱动颗粒的气化。 现场燃料合成反应器可以从气化反应中接收氢气和一氧化碳产物，在烃燃料合成过程中使用氢气和一氧化碳产物以产生液态烃燃料。
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