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41. 发明授权

US09388046B2 Systems and apparatus for production of high-carbon biogenic reagents 有权
标题翻译：用于生产高碳生物试剂的系统和设备
公开(公告)号：US09388046B2
公开(公告)日：2016-07-12
申请号：US14111281
申请日：2012-04-13
申请人： James A. Mennell , Daniel J. Despen
发明人： James A. Mennell , Daniel J. Despen
IPC分类号： C10L9/00 , C01B31/02 , C10B49/02 , C10B53/02 , C10B57/02 , C10L5/04 , C10L5/44 , C10B39/00 , C10B47/30 , C10B43/02 , B01J21/18 , C01B31/08 , C10L5/36 , C21C5/52 , C22B4/02 , H01B1/04 , C21B5/00 , C21B13/00
CPC分类号： C10L5/447 , B01J21/18 , C01B32/30 , C01B32/312 , C01B32/318 , C10B39/00 , C10B39/02 , C10B41/00 , C10B43/02 , C10B45/00 , C10B47/30 , C10B49/02 , C10B53/02 , C10B57/02 , C10B57/06 , C10B57/10 , C10L5/04 , C10L5/36 , C10L5/363 , C10L5/365 , C10L5/366 , C10L5/442 , C10L2200/0204 , C10L2200/025 , C10L2200/0469 , C10L2290/02 , C10L2290/06 , C10L2290/08 , C10L2290/145 , C10L2290/28 , C10L2290/30 , C10L2290/50 , C10L2290/52 , C10L2290/58 , C10L2290/60 , C21B5/007 , C21B13/0066 , C21C5/52 , C22B4/02 , H01B1/04 , Y02E50/10 , Y02E50/14 , Y02E50/30 , Y02E50/32 , Y02P10/143 , Y02P20/129 , Y02P20/145 , Y02W10/30 , Y02W10/37
摘要： This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu/lb, 13,000 Btu/lb, 14,000 Btu/lb, or 14,500 Btu/lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and/or strength that derive from the feedstock, heat rate, and additives.
摘要翻译：本发明提供了将生物质转化成适用于各种商业应用的高碳生物源试剂的方法和系统。一些实施例在惰性气体存在下采用热解产生热的热解固体，可冷凝的蒸气和不可冷凝的气体，然后分离出蒸气和气体，并在惰性气体存在下冷却热的热解固体。可以在加工过程中引入添加剂或与试剂或二者结合。生物源试剂可以包括至少70重量％，80重量％，90重量％，95重量％或更多的总碳。生物制剂可以具有至少12,000Btu / lb，13,000Btu / lb，14,000Btu / lb或14,500Btu / lb的能量含量。生物制剂可以形成细粉末或结构物。结构物体可以具有源自原料，加热速率和添加剂的结构和/或强度。

42. 发明授权

US09382482B2 Continuous liquid fuel production methods, systems, and devices 有权
标题翻译：连续液体燃料生产方法，系统和装置
公开(公告)号：US09382482B2
公开(公告)日：2016-07-05
申请号：US14638992
申请日：2015-03-04
申请人： Proton Power, Inc.
发明人： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver
IPC分类号： C01B3/00 , C01B3/02 , C01B3/32 , C01B3/34 , C01B3/46 , C10K3/00 , C10K3/06 , C10B47/00 , C10B49/02 , C10B53/02 , C10B57/00 , C10B57/02 , C10L1/02 , C10L1/04 , C11B1/12 , C10B49/00 , C10B53/00 , C10L1/00 , C10L1/10 , C10L1/12
CPC分类号： C10B53/02 , C10B47/00 , C10B49/02 , C10B57/005 , C10B57/02 , C10G49/007 , C10G2300/1011 , C10G2300/4037 , C10G2300/42 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10K3/06 , C10L1/02 , C10L1/04 , C10L2200/0469 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/02 , C10L2290/08 , C11B1/12 , Y02E50/14 , Y02E50/32 , Y02P30/20 , Y02T50/678
摘要： Methods, systems, and devices for continuous fuel production are provided. Some embodiments may utilize two pyrolysis platforms, which may utilize biomass as a feedstock. One platform may generally utilize a high temperature pyrolysis process that may generate at least hydrogen and carbon monoxide. This high temperature gas stream may be fed into a lower temperature fast pyrolysis stream as a cover gas. The hot cover gas may react with the fast pyrolysis vapors hydrotreating while the vapors may still be hot and the molecules may still be small. The reacted product may then be distilled on the cool down. This may provide a rapid continuous process for the production of liquid fuels from biomass or other compounds that include carbon-oxygen-hydrogen (C—O—H) compounds.
摘要翻译：提供了连续燃料生产的方法，系统和设备。一些实施方案可以利用可利用生物质作为原料的两个热解平台。一个平台通常可以利用可产生至少氢和一氧化碳的高温热解过程。这种高温气流可以作为覆盖气体进料到较低温度的快速热解流中。热覆盖气体可以与快速热解蒸气加氢处理反应，同时蒸气仍然是热的，并且分子可能仍然很小。然后将反应的产物在冷却下蒸馏。这可以提供用于从生物质或包括碳 - 氧 - 氢（C-O-H）化合物的其它化合物生产液体燃料的快速连续方法。

43. 发明申请

US20160130503A1 APPARATUS FOR ENDOTHERMIC REACTIONS 审中-公开
标题翻译：用于内热反应的装置
公开(公告)号：US20160130503A1
公开(公告)日：2016-05-12
申请号：US14898116
申请日：2014-06-13
申请人： UNIVERSITY OF PRETORIA
发明人： Michael David Heydenrych
IPC分类号： C10B49/22 , C10B57/02 , C10B57/06 , C10B53/02
CPC分类号： C10B49/22 , B01J8/002 , B01J8/1809 , B01J8/1827 , B01J8/1872 , B01J8/26 , B01J2208/00212 , B01J2208/00274 , B01J2208/00761 , B01J2208/0084 , B01J2208/00902 , B01J2208/00938 , C10B53/02 , C10B57/02 , C10B57/06 , C10J3/463 , C10J2200/152 , C10J2300/0916 , C10J2300/0946 , C10J2300/0976 , C10J2300/0996 , C10J2300/1637 , C10J2300/1687 , C10J2300/1807 , C10J2300/1853 , C10J2300/1876 , F23C10/005 , F23C10/01 , F23G5/0276 , F23G5/30 , F23G2201/301 , F23G2201/304 , F23G2900/50202 , Y02E50/14
摘要： The invention provides an apparatus which consists of two fluidised beds 1 and 2 separated by a vertical divides'5. A positive displacement device such as an auger 3 moves the bed material from the reduction side to the combustion side of the device below the fluidisation zone. The height of the two fluidised beds is equalised by movement of the bed material through a hole 4 In the vertical divider, from the high temperature side 1 (zone 1) to the tow temperature side 2 (zone 2). The bed material that moves through the hole 4 provides energy to drive reactions that may occur on the reduction side. Energy may also be provided to zone 2 by means of conductive and radiative heat transfer through the dividing wall 5. Energy is provided to zone 1 by means of an exothermic reaction, typically combustion of a fuel 13 using air 12.
摘要翻译：本发明提供了一种装置，其由两个被垂直分隔的分离的流化床1和2组成。诸如螺旋推运器3的正位移装置将床材料从装置的还原侧移动到流化区下方的燃烧侧。通过床材料通过孔4的移动使两个流化床的高度相等。在垂直分隔器中，从高温侧1（区域1）到丝束温度侧2（区域2）。通过孔4移动的床材料提供能量以驱动可能在还原侧发生的反应。也可以通过通过分隔壁5的导电和辐射热传递将能量提供给区域2.通过放热反应（通常使用空气12燃料13的燃烧）将能量提供给区域1。

44. 发明授权

US09321966B2 Method for carbonization of crop straws 有权
标题翻译：农作物秸秆碳化方法
公开(公告)号：US09321966B2
公开(公告)日：2016-04-26
申请号：US13579147
申请日：2011-02-21
申请人： Xiaoguang Wang , Jingyong Jing , Shuqin Zhang
发明人： Xiaoguang Wang , Jingyong Jing , Shuqin Zhang
IPC分类号： C10B53/02 , C10B49/02 , C10B57/02 , C01B31/02 , C10G1/02 , C10L5/44
CPC分类号： C10B53/02 , C01B32/05 , C05D9/00 , C10B49/02 , C10B57/02 , C10G1/02 , C10L5/447 , C10L2200/0469 , C10L2290/02 , Y02E50/10 , Y02E50/14 , Y02E50/30
摘要： The present invention is to provide a method for carbonification of crop straws and a device thereof. Pyrolysis process is controlled by regulating the feeding of oxygen during said pyrolysis process, and pyrolysis and carbonification are respectively conducted in separate pyrolysis and carbonification pools, wherein the straws are pyrolyzed in said pyrolysis pool and entered into said carbonification pool to be carbonified. The present invention can quickly raise the temperature of the pyrolysis process, shorten the time of the pyrolysis process, and improve the pyrolysis carbonification efficiency.
摘要翻译：本发明提供一种农作物秸秆的碳化方法及其装置。通过在所述热解过程中调节氧气的供给来控制热解过程，热解和碳化分别在分离的热解和碳化池中进行，其中吸管在所述热解池中热解并进入所述碳化池以进行碳化。本发明可以快速提高热解过程的温度，缩短热解过程的时间，提高热解碳化效率。

45. 发明申请

US20150218456A1 APPARATUS AND METHODS FOR GASIFICATION 审中-公开
标题翻译：装置和方法用于气化
公开(公告)号：US20150218456A1
公开(公告)日：2015-08-06
申请号：US14415062
申请日：2013-07-17
申请人： Pyroneer A/S
发明人： Rasmus Glar Nielsen , Peder Christian Stoholm
IPC分类号： C10B49/22 , C10B57/02 , C10B27/06 , C10B53/02
CPC分类号： C10B49/22 , C10B27/06 , C10B53/02 , C10B57/02 , C10J3/482 , C10J3/54 , C10J3/62 , C10J3/721 , C10J2300/094 , C10J2300/0956 , C10J2300/0976 , C10J2300/0993 , C10J2300/1807 , C10K1/026 , F23C10/10 , Y02E50/14
摘要： The invention relates to a circulating fluidized bed (CFB) reactor for thermal processing of added carbonaceous material, the carbonaceous material normally comprises organic material or organic material mixed with inorganic material such as in straw or other vegetable waste, manure, household rubbish, dried wastewater, dried animal remains or other dried carbonaceous waste products. The invention also relates to a process for manufacturing a combustible product gas having a heating value around 4-8 MJ/Nm3 from such a carbonaceous material by subjecting the carbonaceous material to pyrolysis in one process step and oxidation in two subsequent process steps. A circulating fluidized bed (CFB) reactor according to the invention comprises a primary char gasification chamber (5) and an intermediate char gasification chamber (9) typically provided with a fluidized bed wherein the height (h10) of the second fluidized bed (10) in the intermediate char gasification chamber is larger than the height (hn) of the first fluidized bed (11) in the primary char gasification chamber (5).
摘要翻译：本发明涉及一种用于热加工添加碳质材料的循环流化床（CFB）反应器，碳质材料通常包括有机材料或与无机材料混合的有机材料，如秸秆或其他蔬菜废物，粪便，家用垃圾，干燥废水，干燥的动物遗体或其他干燥的含碳废物。本发明还涉及通过在一个工艺步骤中对含碳材料进行热解并在两个后续工艺步骤中进行氧化来制造具有约4-8MJ / Nm3的加热值的可燃产品气体的方法。根据本发明的循环流化床（CFB）反应器包括主要气化室（5）和通常设置有流化床的中间焦化气化室（9），其中第二流化床（10）的高度（h10）在中间焦化气化室中比主炭气化室（5）中的第一流化床（11）的高度（hn）大。

46. 发明授权

US08030420B2 Olefin polymerization reaction unit and polyolefin production process 有权
标题翻译：烯烃聚合反应单元和聚烯烃生产工艺
公开(公告)号：US08030420B2
公开(公告)日：2011-10-04
申请号：US12332065
申请日：2008-12-10
申请人： Hiroyuki Ogawa , Hideki Sato
发明人： Hiroyuki Ogawa , Hideki Sato
IPC分类号： C08F2/00 , C10B57/02
CPC分类号： C08F10/00 , C08F2/34 , C08F2/001
摘要： An olefin polymerization reaction unit includes a multistage gas phase polymerization reactor which is divided into two or more polymerization stages, in which polyolefin particles move from an initial stage to a final stage, and in which an olefin monomer-containing gas is fed from the final stage toward the initial stage. The reaction unit also includes first circulating means for feeding to the final stage a gas that is discharged from the initial stage and then cooled with a first heat exchanger, and second circulating means for feeding to one of the polymerization stages a condensate formed by condensing, with a second heat exchanger different from the first heat exchanger, a gas removed from one of the polymerization stages.
摘要翻译：烯烃聚合反应单元包括多级气相聚合反应器，其分为两个或多个聚合阶段，其中聚烯烃颗粒从初始阶段移动到最终阶段，并且其中含有烯烃单体的气体从最终的阶段到初始阶段。反应单元还包括第一循环装置，用于将从初始阶段排放然后用第一热交换器冷却的气体进料到最终级，以及第二循环装置，用于将通过冷凝形成的冷凝物进料到一个聚合阶段，与不同于第一热交换器的第二热交换器从一个聚合阶段除去气体。

47. 发明授权

US08025858B2 Apparatus and process for light olefin recovery 有权
标题翻译：轻烯烃回收的设备和工艺
公开(公告)号：US08025858B2
公开(公告)日：2011-09-27
申请号：US11828433
申请日：2007-07-26
申请人： Douglas G. Stewart , Joseph E. Zimmermann , Angelo P. Furfaro , Bipin V. Vora
发明人： Douglas G. Stewart , Joseph E. Zimmermann , Angelo P. Furfaro , Bipin V. Vora
IPC分类号： B01J8/04 , C07C1/00 , C10B57/02
CPC分类号： C07C4/06 , C07C7/163 , C10G2400/20 , Y02P30/42 , C07C11/04 , C07C11/06 , C07C11/02
摘要： The present invention relates to a process and apparatus for the production of light olefins comprising olefins having from 2 to 3 carbon atoms per molecule from a feedstock containing heavier olefins. An intermediate cut from a fractionation column is used as olefinic feed to an olefin cracking process preferably after undergoing selective hydrogenation of diolefins. In one embodiment, a liquid side draw from a fractionation column is selectively hydrogenated and then returned to the fractionation column from which a vapor side draw containing olefins is cracked in the olefin cracking reactor.
摘要翻译：本发明涉及一种用于生产轻质烯烃的方法和设备，其包含每分子含有2至3个碳原子的烯烃，其含有较重的烯烃的原料。来自分馏塔的中间馏分用作烯烃裂化方法的烯烃进料，优选在进行二烯烃的选择性氢化之后。在一个实施方案中，从分馏塔抽出的液体侧被选择性氢化，然后返回到在烯烃裂解反应器中含有烯烃的蒸汽侧馏分从其分馏的分馏塔。

48. 发明授权

US07884138B2 Process for making Fischer-Tropsch olefinic naphtha and hydrogenated distillates 有权
标题翻译：制备费 - 托烯烃石脑油和氢化馏分的方法
公开(公告)号：US07884138B2
公开(公告)日：2011-02-08
申请号：US11956455
申请日：2007-12-14
申请人： Jerome F. Mayer , Dennis J. O'Rear
发明人： Jerome F. Mayer , Dennis J. O'Rear
IPC分类号： C07C27/00 , C10B57/02
CPC分类号： C10G2/32 , C10G2400/20
摘要： A process is described by which an olefinic naphtha and a hydrogenated distillate fuel are made from a Fischer-Tropsch process. The olefinic naphtha is suitable for use in an ethylene cracker where the olefins enhance the formation of ethylene. Thy hydrogenated distillate fuel is used in jet and or diesel fuels. Optionally the olefinic naphtha has a low content of acids. This low acid content, is obtained by operating the Fischer-Tropsch unit at H2/CO ratios from 1.8 to 2.05 or treating the effluent from the Fischer-Tropsch unit with a metal oxide to remove the acids.
摘要翻译：描述了由费 - 托法制备烯烃石脑油和氢化馏出物燃料的方法。烯烃石脑油适用于乙烯裂化器，其中烯烃增强了乙烯的形成。氢化的馏分燃料用于喷气和/或柴油。任选地，烯烃石脑油具有低含量的酸。这种低酸含量是通过以1.8至2.05的H 2 / CO比操作费 - 托单元或用金属氧化物处理来自费 - 托单元的流出物以除去酸而获得的。

49. 发明授权

US07727377B2 System and process for the treatment of multiphase residues 有权
标题翻译：用于处理多相残留物的系统和方法
公开(公告)号：US07727377B2
公开(公告)日：2010-06-01
申请号：US11074748
申请日：2005-03-09
申请人： Arilza de Castilho Pickler , Luis Fernando Piexoto Gallo , Carlos Alberto Dias da Silva , Waldir Albrecht , Christine Albrecht Althoff
发明人： Arilza de Castilho Pickler , Luis Fernando Piexoto Gallo , Carlos Alberto Dias da Silva , Waldir Albrecht , Christine Albrecht Althoff
IPC分类号： C10B57/02 , C11B1/00 , C02F1/68 , C10G1/00 , F28D21/00
CPC分类号： C10G1/02 , C10B47/44 , C10B53/00 , C10B53/07 , C10B57/02 , Y02P20/143
摘要： A system 100 is described for the treatment of multiphase residues having unlimited content of water, oil and solids to obtain hydrocarbons and other products, said system comprising multiphase residue feed system 10, inert gas system 20 and reduced pressure system 30, tubular reactor 40 provided with three heating zones Z-1, Z-2 and Z-3 with a temperature gradient and transportation helicoid 42 to displace the residue mass throughout the reaction zones, the hydrocarbon products and water being collected in a system 60 of condensers 61, 62 and 63 linked to a system 70 of bubbling vessels 71, 72 and 73, reactor 40 being operated in the sealed mode and being provided with a multiphase residue inlet 43 and exit 44 of solid product. The solid product is collected in a system 50 comprising upper valve 51 and lower valve 52, and intermediate silo 53 and then directed to post-treatment system 90 for activation aiming at industrial utilization. The process using the system 100 of the invention is also described. Multiphase organic residues, petroleum residues, pure or in admixture in any amount, from chemical and pharmaceutical industries, paper and pulp industry, and mining industries can be processed in the inventive system. Besides, it is possible to recover phenols from foundry sands in the system and process described.
摘要翻译：描述了用于处理具有无限含量的水，油和固体的多相残留物以获得烃和其它产物的系统100，所述系统包括多相残余物进料系统10，惰性气体系统20和减压系统30，提供的管式反应器40 具有温度梯度和输送螺旋体42的三个加热区Z-1，Z-2和Z-3，以将整个反应区中的残余物质置换，将烃产物和水收集在冷凝器61,62的系统60中， 63连接到鼓泡容器71,72和73的系统70，反应器40以密封模式操作并且设置有多相残留物入口43和固体产物的出口44。将固体产物收集在包括上阀51和下阀52以及中间仓53的系统50中，然后被引导到后处理系统90以用于工业利用。还描述了使用本发明的系统100的过程。可以在本发明的系统中处理来自化学和制药工业，造纸和纸浆工业以及采矿业的多相有机残余物，石油残余物，纯的或以任何量混合的混合物。此外，可以在所述的系统和方法中从铸造砂中回收苯酚。

50. 发明申请

US20050072343A1 Process for carbonizing wood residues and producing activated carbon 失效
标题翻译：碳化残余木炭和生产活性炭的方法
公开(公告)号：US20050072343A1
公开(公告)日：2005-04-07
申请号：US10933312
申请日：2004-09-03
申请人： Paul Fung , Adrian De Vos , Velauthapillai Muruganathan , Hoc Ng
发明人： Paul Fung , Adrian De Vos , Velauthapillai Muruganathan , Hoc Ng
IPC分类号： C01B31/02 , C01B31/10 , C10B49/10 , C10B49/22 , C10B53/02 , C10B57/02 , F23G5/00 , F23G7/00
CPC分类号： C10B57/02 , C01B32/336 , C10B49/10 , C10B49/22 , C10B53/02 , Y02E50/14 , Y02P20/129 , Y02P20/145
摘要： An apparatus and process for preparing activated carbon from a wood or wood residue feedstock using fluidized bed technology. The fluidized bed apparatus has a number of wood residue inlets that allow differing residence times in the fluidized bed apparatus appropriate for the wood or wood residue feedstock to be carbonized. The carbonized material may then be activated to form activated carbon.
摘要翻译：使用流化床技术从木材或木材残余物原料制备活性炭的装置和方法。流化床装置具有许多木屑残留物入口，其允许在流化床装置中适合木炭或木材残渣原料被碳化的不同停留时间。然后可以将碳化材料活化以形成活性炭。

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