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81. 发明申请

US20090064584A1 HYDROGEN AND CARBON UTILIZATION IN SYNTHETIC FUELS PRODUCTION PLANTS 有权
标题翻译：合成燃料生产厂的氢和碳利用
公开(公告)号：US20090064584A1
公开(公告)日：2009-03-12
申请号：US12207978
申请日：2008-09-10
申请人： Sergio Mohedas , Mark Ibsen
发明人： Sergio Mohedas , Mark Ibsen
IPC分类号： C10J1/20
CPC分类号： C10J3/00 , B01J37/16 , B01J37/18 , C01B3/34 , C01B3/56 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0485 , C01B2203/049 , C01B2203/062 , C10G2/332 , C10G45/60 , C10G47/02 , C10G49/02 , C10G2300/1011 , C10G2300/703 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/1618 , C10J2300/1659 , C10J2300/1823 , C10K3/00 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A method of utilizing hydrogen in synthesis gas production by forming synthesis gas from one or more carbonaceous materials, the synthesis gas comprising hydrogen and carbon monoxide; separating a hydrogen-rich product and a hydrogen-lean product from the synthesis gas to yield an adjusted synthesis gas product; and activating a hydrocarbon synthesis catalyst with at least a portion of the hydrogen-lean product. A system for carrying out the method is also provided, the system including at least one hydrogen extraction unit and an activation reactor operable to activate hydrocarbon synthesis catalyst, wherein the activation reactor comprises an inlet fluidly connected with the at least one hydrogen extraction unit whereby at least a portion of a hydrogen-lean gas stream, at least a portion of a hydrogen-rich gas stream, or at least a portion of both may be introduced into the activation reactor.
摘要翻译：一种通过从一种或多种含碳材料形成合成气而在合成气生产中利用氢的方法，所述合成气包含氢气和一氧化碳; 从合成气中分离富氢产物和贫氢产物以产生经调节的合成气产物; 以及用至少一部分所述富氢产物活化烃合成催化剂。还提供了一种用于实施该方法的系统，所述系统包括至少一个氢提取单元和可操作以活化烃合成催化剂的活化反应器，其中所述活化反应器包括与所述至少一个氢提取单元流体连接的入口，贫氢气流的至少一部分，富氢气流的至少一部分或两者的至少一部分可以被引入到活化反应器中。

82. 发明申请

US20090064578A1 Biomass Gasifier System with Low Energy and Maintenance Requirements 有权
标题翻译：低能耗和维护要求的生物质气化器系统
公开(公告)号：US20090064578A1
公开(公告)日：2009-03-12
申请号：US12139940
申请日：2008-06-16
申请人： Chandra S. Theegala
发明人： Chandra S. Theegala
IPC分类号： C10J3/68
CPC分类号： C10J3/26 , C10J3/34 , C10J3/80 , C10J3/84 , C10J2200/158 , C10J2300/0916 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/1606 , C10J2300/165 , C10J2300/1659 , Y02E50/32 , Y02P20/145
摘要： A down-draft fixed bed gasifier is disclosed that produced clean producer or synthesis gas. The gasifier can be installed at a stationary location or can be scaled down to enable placing the gasifier on a trailer that can be moved to the site of biomass generation. The gasifier is vertically oriented and generally cylindrical, and the design allows for a continual input of feedstock into the gasifier with less clogging and without lowering the gas pressure inside the gasifier. The design incorporates an internal catalyst to clean tars from the produced gas, and uses heat from the combustion chamber of the gasifier to heat the catalyst. The flow of air may be either positive flow or negative flow.
摘要翻译：公开了一种生产清洁生产者或合成气的下降式固定床气化炉。气化器可以安装在固定的位置，或者可以按比例缩小，以便将气化器放置在可以移动到生物质生产现场的拖车上。气化器是垂直取向的并且通常是圆柱形的，并且该设计允许将原料连续输入到气化器中，具有更少的堵塞并且不降低气化器内的气体压力。该设计结合了内部催化剂，用于清洁来自产生气体的焦油，并且使用来自气化器的燃烧室的热量来加热催化剂。空气流可以是正流量或负流量。

83. 发明申请

US20090049748A1 METHOD AND SYSTEM FOR CONVERTING WASTE INTO ENERGY 审中-公开
标题翻译：将废物转化为能源的方法和系统
公开(公告)号：US20090049748A1
公开(公告)日：2009-02-26
申请号：US12201558
申请日：2008-08-29
申请人： Eric Day , Andrew Eric Day
发明人： Eric Day , Andrew Eric Day
IPC分类号： C10J3/68 , C12M1/00
CPC分类号： C12N1/12 , B01D53/84 , B01D2251/95 , B01D2257/504 , C01B3/342 , C01B3/348 , C01B2203/0283 , C01B2203/0405 , C01B2203/0445 , C01B2203/0475 , C01B2203/062 , C01B2203/0861 , C01B2203/1211 , C01B2203/1235 , C01B2203/84 , C01B2203/86 , C10J3/48 , C10J2300/0916 , C10J2300/0946 , C10J2300/1238 , C10J2300/1659 , C10J2300/1671 , C10J2300/1681 , C10J2300/1693 , C10J2300/1696 , C10J2300/1892 , Y02A50/2358 , Y02E50/32 , Y02P20/145 , Y02P20/152 , Y02P20/59 , Y02P30/30
摘要： Disclosed herein is system comprising a system comprising a high temperature gasifier; the high temperature gasifier being operative to function at temperatures of greater than or equal to about 450° F.; and a synthesizing reactor in fluid communication with the high temperature gasifier; the synthesizing reactor being operative to convert carbon dioxide into another form of carbon. Disclosed herein too a method comprising gasifying a waste stream to produce a composition that comprises syngas; the syngas comprising carbon monoxide and hydrogen; the gasifying being conducted in a high temperature gasifier; the high temperature gasifier being operative to function at temperatures of greater than or equal to about 450° F.; converting the carbon monoxide into carbon dioxide; and feeding the carbon dioxide to an synthesizing reactor to produce an oil rich algae.
摘要翻译：本文公开了包括包括高温气化器的系统的系统; 高温气化器可操作以在大于或等于约450°F的温度下起作用; 和与高温气化器流体连通的合成反应器; 合成反应器可操作以将二氧化碳转化为另一种形式的碳。本文还公开了一种方法，包括气化废物流以产生包含合成气的组合物; 合成气包含一氧化碳和氢气; 气化在高温气化炉中进行; 高温气化器可操作以在大于或等于约450°F的温度下起作用; 将一氧化碳转化为二氧化碳; 并将二氧化碳进料到合成反应器中以产生富含油的藻类。

84. 发明申请

US20090019767A1 HEAT INTEGRATION AND CONDENSATE TREATMENT IN A SHIFT FEED GAS SATURATOR 有权
标题翻译：转炉进料气体加热器中的热量整合和冷凝处理
公开(公告)号：US20090019767A1
公开(公告)日：2009-01-22
申请号：US11831338
申请日：2007-07-31
申请人： JOHN ABUGHAZALEH , SIVA ARIYAPADI
发明人： JOHN ABUGHAZALEH , SIVA ARIYAPADI
IPC分类号： B01J7/02
CPC分类号： C01B3/16 , C01B2203/0283 , C01B2203/0405 , C01B2203/042 , C01B2203/043 , C01B2203/046 , C01B2203/1041 , C01B2203/1047 , C10J3/485 , C10J2300/0959 , C10J2300/1618 , C10J2300/1646 , C10J2300/165 , C10J2300/1659 , C10J2300/1665 , C10J2300/1668 , C10J2300/1671 , C10J2300/1678 , C10J2300/1807 , C10K3/04
摘要： Systems and processes for adjusting hydrogen content of a synthesis gas are provided. At least a portion of carbon monoxide in a syngas can be converted to carbon dioxide to provide a shifted syngas and condensed water. The syngas can have a first hydrogen to carbon monoxide ratio and a first temperature, and the shifted syngas can have a second hydrogen to carbon monoxide ratio and a second temperature, both greater than the first. Heat from the shifted syngas can be at least partially transferred from the shifted syngas to the condensed water to at least partially vaporize the condensed water. The syngas can be at least partially saturated with the at least partially vaporized condensed water. A ratio of the water vapor to syngas can be about 1.0 or less.
摘要翻译：提供了用于调节合成气氢含量的系统和方法。合成气中的一氧化碳的至少一部分可以转化为二氧化碳以提供经转换的合成气和冷凝水。合成气可以具有第一氢气与一氧化碳的比率和第一温度，并且所转移的合成气可以具有第二氢气与一氧化碳的比例，以及第二温度都大于第一温度。来自转移的合成气的热量可以至少部分地从转移的合成气转移到冷凝水中，以至少部分地蒸发冷凝的水。合成气可以至少部分地被至少部分蒸发的冷凝水饱和。水蒸汽与合成气的比可以为约1.0以下。

85. 发明申请

US20090012188A1 Process for the production of synthesis gas with conversion of CO2 into hydrogen 有权
标题翻译：用CO 2转化为氢气生产合成气的方法
公开(公告)号：US20090012188A1
公开(公告)日：2009-01-08
申请号：US11890525
申请日：2007-08-07
申请人： Alexandre Rojey , Reynald Bonneau , Nicolas Boudet
发明人： Alexandre Rojey , Reynald Bonneau , Nicolas Boudet
IPC分类号： C07C27/00
CPC分类号： C01B3/36 , C01B2203/0233 , C01B2203/0255 , C01B2203/062 , C10J3/00 , C10J3/82 , C10J2300/0916 , C10J2300/092 , C10J2300/093 , C10J2300/1659 , C10J2300/1665 , C10J2300/1838 , C10J2300/1846 , C10J2300/1853 , C10K3/026 , Y02E50/18 , Y02P20/129 , Y02P20/145 , Y02P20/146
摘要： Process for the production of liquid hydrocarbons from a feedstock that comprises at least one elementary feedstock from the group of biomass, coal, lignite, petroleum residues, methane, and natural gas, comprising: at least one stage a) for gasification of the feedstock by partial oxidation and/or steam reforming to produce a synthesis gas SG; a stage b) for separating CO2 from SG and a portion of the effluent of the subsequent stage c); the mixing of a portion of the CO2 that is separated with a gas of an H2/CO ratio of more than 3; a stage c) for partial conversion with hydrogen, thermal or thermocatalytic, of the CO2 that is present in said first mixture according to the reaction: CO2+H2→CO+H2O in a specific reaction zone that is separated from said gasification zone or zones; a stage d) for Fisher-Tropsch synthesis on a synthesis gas that comprises at least a portion of SG and at least a portion of the CO that is produced by the conversion of CO2 into hydrogen.
摘要翻译：用于从原料生产液体烃的方法，所述原料包含来自生物质，煤，褐煤，石油残渣，甲烷和天然气组的至少一种基本原料，包括：至少一个阶段a）用于通过部分氧化和/或蒸汽重整以产生合成气SG; 一个阶段b）从SG和后续阶段c）的一部分流出物分离CO 2; 将一部分与H2 / CO比大于3的气体分离的CO 2混合; 根据CO 2 + H 2→CO + H 2 O在与所述气化区分离的特定反应区中，存在于所述第一混合物中的CO 2部分转化为氢，热或热催化的阶段c）区域合成气中的Fisher-Tropsch合成阶段d），其包含至少一部分SG和通过CO 2转化为氢而产生的至少一部分CO。

86. 发明申请

US20080275278A1 Reduced-Emission Gasification and Oxidation of Hydrocarbon Materials for Liquid Fuel Production 有权
标题翻译：用于液体燃料生产的烃类材料的减排气化和氧化
公开(公告)号：US20080275278A1
公开(公告)日：2008-11-06
申请号：US12114820
申请日：2008-05-05
申请人： Steve L. Clark
发明人： Steve L. Clark
IPC分类号： C10G1/00 , B01J8/04
CPC分类号： C10J3/00 , C10G2/32 , C10J3/721 , C10J2300/0916 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1606 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10J2300/1684 , C10J2300/1687 , C10K1/003 , C10K1/02 , C10K1/024 , C10K1/028 , C10K1/12 , C10K1/32
摘要： A system and process are disclosed for the controlled combustion of a wide variety of hydrocarbon feedstocks to produce thermal energy, liquid fuels, and other valuable products with little or no emissions. The hydrocarbon feeds, such as coal and biomass, are first gasified and then oxidized in a two-chamber system/process using pure oxygen rather than ambient air. A portion of the intermediate gases generated in the system/process are sent to a Fischer-Tropsch synthesis process for conversion into diesel fuel and other desired liquid hydrocarbons. The remaining intermediate gases are circulated and recycled through each of the gasification/oxidation chambers in order to maximize energy production. The energy produced through the system/process is used to generate steam and produce power through conventional steam turbine technology. In addition to the release of heat energy, the hydrocarbon fuels are oxidized to the pure product compounds of water and carbon dioxide, which are subsequently purified and marketed. The system/process minimizes environmental emissions.
摘要翻译：公开了一种系统和方法，用于多种烃原料的受控燃烧以产生具有很少或不具有排放物的热能，液体燃料和其它有价值的产物。碳氢化合物进料如煤和生物质首先被气化，然后在使用纯氧而不是环境空气的两室系统/方法中进行氧化。将系统/方法中产生的一部分中间气体送入费 - 托合成方法，以转化为柴油燃料和其它所需的液态烃。剩余的中间气体通过每个气化/氧化室循环和再循环，以最大限度地提高能量产生。通过系统/过程产生的能量用于通过常规蒸汽轮机技术产生蒸汽并产生电力。除了释放热能之外，烃燃料被氧化成水和二氧化碳的纯产物化合物，随后被纯化和上市。系统/过程最大限度地减少环境排放。

87. 发明申请

US20080262111A1 PROCESS FOR OPERATING A PARTIAL OXIDATION PROCESS OF A SOLID CARBONACEOUS FEED 有权
标题翻译：用于操作固体碳源的部分氧化过程的方法
公开(公告)号：US20080262111A1
公开(公告)日：2008-10-23
申请号：US12101678
申请日：2008-04-11
申请人： Johannes Everdinus Gerrit PLOEG , Jacobus Hendrikus Scheerman
发明人： Johannes Everdinus Gerrit PLOEG , Jacobus Hendrikus Scheerman
IPC分类号： C07C27/12
CPC分类号： C10J3/76 , C10J3/485 , C10J3/506 , C10J3/723 , C10J3/84 , C10J3/86 , C10J2200/152 , C10J2300/093 , C10J2300/0959 , C10J2300/0969 , C10J2300/1659 , C10J2300/1665 , C10K1/004 , C10K1/006 , C10K1/007 , C10K1/101 , C10K1/165 , C10K3/04
摘要： The invention is directed to a process for preparing a mixture comprising CO and H2 by operating a partial oxidation process of a solid carbonaceous feed, which process comprises the steps of: (a) supplying the solid carbonaceous feed and an oxygen-containing stream to a burner, wherein a CO2 containing transport gas is used to transport the solid carbonaceous feed to the burner; (b) partially oxidising the carbonaceous feed in the burner wherein a gaseous stream comprising CO and H2 is being discharged from said burner into a reaction zone, wherein the temperature in the reaction zone is from 1200 to 1800° C. and wherein said reaction zone is at least partly bounded by a wall, which wall comprises conduits in which steam is prepared by evaporation of water, resulting in a flow of steam being discharged from said reaction zone; (c) monitoring the conditions in the reaction zone by continually or periodically measuring the rate of the steam flow and using said flow rate as input to adjust the oxygen-to-coal (O/C) ratio in step (a).
摘要翻译：本发明涉及通过操作固体碳质饲料的部分氧化方法来制备包含CO和H 2 O 2的混合物的方法，该方法包括以下步骤：（a）将固体碳质饲料和含氧物流到燃烧器，其中使用含CO 2的运输气体将固体碳质进料运送到燃烧器; （b）部分氧化燃烧器中的含碳进料，其中包含CO和H 2的气态物流从所述燃烧器排放到反应区中，其中反应区中的温度为1200至1800 其中所述反应区至少部分地由壁限定，所述壁包括导管，其中通过蒸发水制备蒸汽，导致从所述反应区排出的蒸汽流; （c）通过连续或周期性地测量蒸汽流量的速率来监测反应区中的条件，并使用所述流速作为输入调节步骤（a）中的氧 - 煤（O / C）比。

88. 发明申请

US20080202028A1 System For the Conversion of Carbonaceous Fbedstocks to a Gas of a Specified Composition 审中-公开
标题翻译：将碳质床垫转化为指定组合物的气体的系统
公开(公告)号：US20080202028A1
公开(公告)日：2008-08-28
申请号：US11916417
申请日：2006-06-05
申请人： Andreas Tsangaris , Kenneth C Campbell , D Michael Feasby , Ke Li
发明人： Andreas Tsangaris , Kenneth C Campbell , D Michael Feasby , Ke Li
IPC分类号： C10J3/16
CPC分类号： C10J3/16 , C10J3/005 , C10J3/18 , C10J3/463 , C10J3/721 , C10J3/723 , C10J2300/06 , C10J2300/093 , C10J2300/0959 , C10J2300/0973 , C10J2300/1238 , C10J2300/1618 , C10J2300/1621 , C10J2300/1646 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10J2300/1693 , C10J2300/1869 , C10J2300/1884 , F23G2204/201 , Y02E20/18 , Y02P20/129 , Y02P20/13
摘要： The present invention provides a carbonaceous feedstock gasification system with integrated control subsystem. The system generally comprises, in various combinations, a gasification reactor vessel (or converter) having one or more processing zones and one or more plasma heat sources, a solid residue handling subsystem, a gas quality conditioning subsystem, as well as an integrated control subsystem for managing the overall energetics of the conversion of the carbonaceous feedstock to energy, as well as maintaining all aspects of the gasification processes at an optimal set point. The gasification system may also optionally comprise a heat recovery subsystem and/or a product gas regulating subsystem.
摘要翻译：本发明提供一种具有综合控制子系统的碳质原料气化系统。该系统通常包括具有一个或多个处理区和一个或多个等离子体热源的气化反应器容器（或转换器），固体残余物处理子系统，气体质量调节子系统以及集成控制子系统用于管理碳质原料转化为能量的总体能量，以及将气化过程的所有方面保持在最佳设定点。气化系统还可以任选地包括热回收子系统和/或产品气体调节子系统。

89. 发明申请

US20080021123A1 Method and apparatus for steam hydro-gasification in a fluidized bed reactor 有权
标题翻译：流化床反应器中蒸汽加氢气化的方法和装置
公开(公告)号：US20080021123A1
公开(公告)日：2008-01-24
申请号：US11879267
申请日：2007-07-16
申请人： Joseph M. Norbeck , Chan Seung Park , Surinder P. Singh
发明人： Joseph M. Norbeck , Chan Seung Park , Surinder P. Singh
IPC分类号： C07C27/06 , F27B15/00
CPC分类号： C01B3/34 , C01B2203/0233 , C01B2203/062 , C01B2203/0838 , C01B2203/1241 , C01B2203/148 , C01B2203/84 , C10G2/32 , C10J3/005 , C10J3/463 , C10J3/503 , C10J2300/093 , C10J2300/0966 , C10J2300/0973 , C10J2300/1659 , C10K3/00 , Y02E20/18 , Y02E50/32
摘要： A method and apparatus for converting carbonaceous material to a stream of methane and carbon monoxide rich gas by heating the carbonaceous material in a fluidized bed reactor using hydrogen, as fluidizing medium, and using steam, under reducing conditions at a temperature and pressure sufficient to generate a stream of methane and carbon monoxide rich gas but at a temperature low enough and/or at a pressure high enough to enable the carbonaceous material to be fluidized by the hydrogen. In particular embodiments, the carbonaceous material is fed as a slurry feed, along with hydrogen, to a kiln type reactor before being fed to the fluidized bed reactor. Apparatus is provided comprising a kiln type reactor, a slurry pump connected to an input of the kiln type reactor, means for connecting a source of hydrogen to an input of the kiln type reactor; a fluidized bed reactor connected to receive output of the kiln type reactor for processing at a fluidizing zone, and a source of steam and a source of hydrogen connected to the fluidized bed reactor below the fluidizing zone. Optionally, a grinder can be provided in the kiln type reactor.
摘要翻译：一种通过在流化床反应器中使用氢气作为流化介质，并且在还原条件下在足以产生的温度和压力下使用蒸汽加热碳质材料，将含碳材料转化为甲烷和一氧化碳富含气流的方法和装置一种富含甲烷和一氧化碳的气体，但在足够低的温度和/或足够高的压力下使含碳材料能够被氢气流化。在具体的实施方案中，碳质材料在加入到流化床反应器之前作为浆料进料以及氢气供入到窑式反应器中。提供了包括窑式反应器，连接到窑式反应器的输入端的浆料泵的装置，用于将氢源连接到窑式反应器的输入端的装置; 连接以接收在流化区处理的窑式反应器的输出的流化床反应器，以及连接到流化床下方的流化床反应器的蒸汽源和氢源。任选地，可以在窑式反应器中提供研磨机。

90. 发明申请

US20070256360A1 METHOD FOR THE GASIFICATION OF MOISTURE-CONTAINING HYDROCARBON FEEDSTOCKS 审中-公开
标题翻译：含水含油物料的气化方法
公开(公告)号：US20070256360A1
公开(公告)日：2007-11-08
申请号：US11746034
申请日：2007-05-08
申请人： James Kindig , Steven Styer
发明人： James Kindig , Steven Styer
IPC分类号： C10J3/00 , C10J3/57
CPC分类号： C10J3/57 , C01B2203/84 , C10J2300/1618 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1693 , C10K1/004 , C10K3/04 , Y02E20/16 , Y02E20/18 , Y02E50/32
摘要： A method for the gasification of a hydrocarbon feedstock that has a high moisture content to produce useful co-products such as high-value hydrocarbon fuels, pure H2, electricity, and/or ammonia. The method advantageously gasifies the carbon in the feedstock to carbon monoxide (CO) without producing large quantities of carbon dioxide (CO2). Supplemental hydrogen (H2) is co-produced by reacting steam (H2O) generated from the moisture in the hydrocarbon feedstock with a molten metal.
摘要翻译：用于气化具有高水分含量的烃原料以产生有用的共同产物如高价值烃燃料，纯H 2，电和/或氨的方法。该方法有利地将原料中的碳气化为一氧化碳（CO），而不产生大量的二氧化碳（CO 2）。通过使来自烃原料中的水分产生的蒸汽（H 2 O 2 O）与熔融金属反应来共同制备补氢（H 2 O 2）。

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