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31. 发明申请

US20170058222A1 FUELS AND FUEL ADDITIVES THAT HAVE HIGH BIOGENIC CONTENT DERIVED FROM RENEWABLE ORGANIC FEEDSTOCK 审中-公开
标题翻译：燃料和燃料添加剂具有从可再生有机饲料得到的高生物量含量
公开(公告)号：US20170058222A1
公开(公告)日：2017-03-02
申请号：US14947820
申请日：2015-11-20
申请人： Fulcrum BioEnergy, Inc.
发明人： Stephen H. Lucas , Peter G. Tiverios , Lewis L. Rich
IPC分类号： C10L1/04 , C10G2/00 , C10K1/00 , C10J3/82 , C10K3/00 , C10L1/08 , C10G47/00
CPC分类号： C10L1/04 , B01J19/0006 , C07C29/1518 , C10G2/32 , C10G2/34 , C10G47/00 , C10J3/26 , C10J3/466 , C10J3/485 , C10J3/721 , C10J3/82 , C10J2300/0903 , C10J2300/0906 , C10J2300/0946 , C10J2300/0959 , C10J2300/0976 , C10J2300/1628 , C10J2300/1634 , C10J2300/1643 , C10J2300/1659 , C10J2300/1665 , C10J2300/1671 , C10J2300/1675 , C10J2300/1815 , C10J2300/1853 , C10K1/004 , C10K1/005 , C10K1/101 , C10K1/16 , C10K3/001 , C10K3/04 , C10L1/08 , C10L2200/0469 , C10L2200/0492 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/04 , C10L2290/10 , C10L2290/42 , C10L2290/54 , C10L2290/543 , Y02E20/16 , Y02E50/18 , Y02E50/32 , Y02E50/343 , Y02P20/129 , Y02P20/133 , Y02P30/10 , C07C31/04 , C07C31/08
摘要： Fuel and fuel additives can be produced by processes that provide Fischer-Tropsch liquids having high biogenic carbon concentrations of up to about 100% biogenic carbon. The fuels and fuel additive have essentially the same high biogenic concentration as the Fischer-Tropsch liquids which, in turn, contain the same concentration of biogenic carbon as the feedstock.
摘要翻译：燃料和燃料添加剂可以通过提供具有高达约100％生物来源碳的高生物碳浓度的费 - 托液体的方法生产。燃料和燃料添加剂与费 - 托液体具有基本上相同的高生物来源浓度，而费 - 托液体又含有与原料相同浓度的生物碳。

32. 发明授权

US09553321B2 Integrated power generation and carbon capture using fuel cells 有权
标题翻译：使用燃料电池的集成发电和碳捕获
公开(公告)号：US09553321B2
公开(公告)日：2017-01-24
申请号：US14207690
申请日：2014-03-13
申请人： Paul J. Berlowitz , Timothy Andrew Barckholtz , Frank Hershkowitz
发明人： Paul J. Berlowitz , Timothy Andrew Barckholtz , Frank Hershkowitz
IPC分类号： H01M8/06 , F02C3/22 , H01M8/04 , C21B15/00 , C04B7/36 , C01B3/50 , C07C29/151 , C10G2/00 , C07C1/04 , C10K3/04 , C01B3/16 , C25B3/02 , C01B3/34 , H01M8/14
CPC分类号： H01M8/06 , C01B3/16 , C01B3/34 , C01B3/48 , C01B3/50 , C01B2203/00 , C01B2203/02 , C01B2203/0205 , C01B2203/0227 , C01B2203/0233 , C01B2203/0283 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/0495 , C01B2203/061 , C01B2203/062 , C01B2203/066 , C01B2203/067 , C01B2203/068 , C01B2203/1205 , C01B2203/1241 , C01B2203/1247 , C01B2203/148 , C01B2203/84 , C01B2203/86 , C01C1/04 , C04B7/367 , C04B2290/20 , C07C1/0485 , C07C29/1518 , C07C29/152 , C10G2/32 , C10G2/332 , C10G2/34 , C10K3/04 , C21B15/00 , C21B2300/02 , C25B3/02 , F02C3/22 , F02C6/18 , H01M8/04 , H01M8/04097 , H01M8/04111 , H01M8/04156 , H01M8/04761 , H01M8/04805 , H01M8/0612 , H01M8/0618 , H01M8/0625 , H01M8/0631 , H01M8/0637 , H01M8/0662 , H01M8/0668 , H01M8/0687 , H01M8/14 , H01M8/141 , H01M8/145 , H01M2008/147 , H01M2250/10 , H01M2250/407 , H01M2300/0051 , Y02B90/14 , Y02E20/14 , Y02E20/16 , Y02E20/185 , Y02E50/18 , Y02E60/50 , Y02E60/526 , Y02E60/563 , Y02E60/566 , Y02P10/132 , Y02P20/129 , Y02P20/13 , Y02P30/30 , Y02P70/56 , Y02T10/16
摘要： Systems and methods are provided for capturing CO2 from a combustion source using molten carbonate fuel cells (MCFCs). At least a portion of the anode exhaust can be recycled for use as part of anode input stream. This can allow for a reduction in the amount of fuel cell area required for separating CO2 from the combustion source exhaust and/or modifications in how the fuel cells can be operated.
摘要翻译：提供了用于使用熔融碳酸盐燃料电池（MCFC）从燃烧源捕获CO 2的系统和方法。阳极排气的至少一部分可以再循环用作阳极输入流的一部分。这可以减少从燃烧源排气中分离CO 2所需的燃料电池面积的数量和/或如何操作燃料电池的修改。

33. 发明授权

US09522864B2 Process for direct conversion of biomass to liquid fuels and chemicals 有权
标题翻译：将生物质直接转化为液体燃料和化学品的方法
公开(公告)号：US09522864B2
公开(公告)日：2016-12-20
申请号：US14323264
申请日：2014-07-03
申请人： The Regents of the University of California
发明人： Theodore D. Matson , Peter C. Ford , Gerald Macala , Alexei Iretski
IPC分类号： C07C1/00 , C07C29/151 , C01B3/22 , C10J3/00 , C10L1/02 , B01J23/80
CPC分类号： C07C29/1518 , B01J23/80 , C01B3/22 , C01B2203/0277 , C01B2203/0283 , C01B2203/1041 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1223 , C10G2300/1011 , C10J3/00 , C10J2300/0916 , C10J2300/0986 , C10J2300/0989 , C10L1/02 , Y02E50/18 , Y02E50/32 , Y02P20/52 , Y02P30/20
摘要： A method of catalytically preparing a fluid product from solid carbonaceous material is described. In the method, at least one of the following equilibria is established by one or more catalysts: a) CH3OH═CO+2H2, b) CO+H2O═CO2+H2. In some versions, the solid carbonaceous material is woody biomass. Components of the fluid product can include one or a combination of C5-C9 alcohols. In certain versions, the method can he practiced with substantially all of the carbon in the carbonaceous material being converted to the fluid product. Also, in some versions, the fluid product can be prepared with substantially no char formation. The fluid product of various versions can be used directly as fuel or as a reagent for preparing commodity chemicals without the need for separating the fluid product components.
摘要翻译：描述了从固体碳质材料催化制备流体产物的方法。在该方法中，通过一种或多种催化剂建立以下平衡中的至少一种：a）CH 3 OH = CO + 2H 2，b）CO + H 2 O = CO 2 + H 2。在一些版本中，固体含碳材料是木质生物质。流体产物的组分可以包括一种或其组合的C5-C9醇。在某些形式中，该方法可以用碳质材料中的基本上所有碳转化为流体产物来实施。而且，在一些形式中，流体产品可以基本上不形成炭黑来制备。各种形式的流体产品可以直接用作燃料或用作制备商品化学品的试剂，而不需要分离流体产物组分。

34. 发明授权

US09505702B2 Integrated process for the production of methyl acetate and methanol from synthesis gas and dimethylether 有权
标题翻译：从合成气和二甲醚生产乙酸甲酯和甲醇的综合工艺
公开(公告)号：US09505702B2
公开(公告)日：2016-11-29
申请号：US14650921
申请日：2013-12-19
申请人： BP Chemicals Limited
发明人： Edo Johann Becker , Timothy Crispin Bristow
IPC分类号： C07C67/37 , C07C51/347 , C07C29/154 , C07C29/151
CPC分类号： C07C67/37 , C07C29/1516 , C07C29/1518 , C07C29/154 , C07C51/347 , Y02P20/125 , C07C69/14 , C07C31/04
摘要： Integrated process for the production of methyl acetate and methanol. The process is carried out by carbonylating dimethyl ether with synthesis gas and recovering methanol and unreacted synthesis gas. The recovered synthesis gas is utilized as the sole fresh synthesis gas for methanol synthesis.
摘要翻译：生产乙酸甲酯和甲醇的综合工艺。该方法通过用合成气羰基化二甲醚并回收甲醇和未反应的合成气进行。回收的合成气用作甲醇合成的唯一新鲜合成气。

35. 发明申请

US20160325253A1 PROCESS FOR REFORMING HYDROCARBONS 审中-公开
标题翻译：改造石油烃的方法
公开(公告)号：US20160325253A1
公开(公告)日：2016-11-10
申请号：US15216075
申请日：2016-07-21
申请人： Haldor Topsøe A/S
发明人： Lari Bjerg Knudsen , Martin Frahm Jensen
IPC分类号： B01J7/00 , B01J19/24 , C07C29/151 , C01C1/04 , C10G2/00 , C07C41/01 , B01J19/00 , C01B3/38
CPC分类号： B01J7/00 , B01J19/0046 , B01J19/2445 , B01J19/245 , B01J2219/00087 , B01J2219/00103 , B01J2219/00495 , B01J2219/00585 , B01J2219/0059 , B01J2219/00594 , B01J2219/00756 , B01J2219/24 , C01B3/382 , C01B3/386 , C01B3/388 , C01B2203/0205 , C01B2203/0227 , C01B2203/0233 , C01B2203/0244 , C01B2203/0255 , C01B2203/0261 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0833 , C01B2203/0844 , C01B2203/0883 , C01B2203/0894 , C01B2203/1235 , C01B2203/1258 , C01B2203/141 , C01B2203/142 , C01B2203/143 , C01B2203/1604 , C01C1/04 , C07C29/1518 , C07C41/01 , C10G2/30 , Y02P20/129
摘要： The invention relates to the production of synthesis gas by means of particularly a series arrangement of heat exchange reforming and autothermal reforming stages, in which the heat required for the reforming reactions in the heat exchange reforming stage is provided by hot effluent synthesis gas from the autothermal reforming stage. More particularly, the invention relates to optimisation of the operation and control of an arrangement of heat exchange reforming and autothermal reforming stages and introduction of an additional waste heat boiler.
摘要翻译：本发明涉及通过特别是热交换重整和自热重整阶段的串联布置来生产合成气，其中热交换重整阶段中的重整反应所需的热量由来自自热的热流出物合成气提供改革阶段更具体地，本发明涉及优化热交换重整和自热重整阶段的布置的操作和控制以及引入另外的废热锅炉。

36. 发明申请

US20160280618A1 METHOD FOR CARBON DIOXIDE HYDROGENATION OF SYNGAS AND THE INTEGRATION OF THE PROCESS WITH SYNGAS CONVERSION PROCESSES 有权
标题翻译：二氧化碳加氢法合成方法和方法与SYNGAS转换方法的整合
公开(公告)号：US20160280618A1
公开(公告)日：2016-09-29
申请号：US15033255
申请日：2014-10-29
申请人： SAUDI BASIC INDUSTRIES CORPORATION
发明人： Aghaddin Mamedov , Clark Rea
IPC分类号： C07C29/151 , C01B3/38
CPC分类号： C07C29/1518 , B01J23/26 , B01J23/34 , B01J23/883 , C01B3/38 , C01B3/382 , C01B3/386 , C01B2203/0233 , C01B2203/0495 , C01B2203/061 , C01B2203/0833 , C01B2203/1058 , C01B2203/1241 , Y02P20/142 , Y02P20/52 , Y02P20/582 , C07C31/04
摘要： Techniques for synthesizing methanol are provided. In an exemplary embodiment, the processes include obtaining a syngas mixture from an integrated carbon dioxide hydrogenation process and a methane steam reforming process, and contacting the syngas mixture with a methanol catalyst to obtain a product stream comprising methanol.
摘要翻译：提供了合成甲醇的技术。在一个示例性实施方案中，所述方法包括从综合二氧化碳氢化方法和甲烷蒸汽重整方法获得合成气混合物，并使合成气混合物与甲醇催化剂接触以获得包含甲醇的产物流。

37. 发明申请

US20160272562A1 METHOD FOR HYDROGENATION OF CO2 IN ADIABATIC METAL REACTORS 有权
标题翻译：在金属反应器中加氢二氧化碳的方法
公开(公告)号：US20160272562A1
公开(公告)日：2016-09-22
申请号：US15034937
申请日：2014-11-06
申请人： SAUDI BASIC INDUSTRIES CORPORATION
发明人： Aghaddin Kh. Mammadov , Clark David Rea
IPC分类号： C07C29/151 , C01B3/58
CPC分类号： C07C29/1518 , B01J8/02 , B01J19/02 , B01J23/14 , B01J23/22 , B01J23/24 , B01J23/34 , B01J33/00 , B01J37/20 , B01J2219/0286 , C01B3/16 , C01B3/58 , C01B32/40 , C01B2203/0435 , C01B2203/0475 , C01B2203/061 , C10K3/026 , C10K3/06 , Y02P20/52
摘要： In an embodiment: a method of making syngas in a metal reactor can comprise introducing carbon dioxide and hydrogen to the metal reactor in the presence of a catalyst to form the syngas, wherein the metal reactor comprises nickel and wherein the carbon dioxide and the hydrogen are in physical contact with a wall of the metal reactor; and passivating the nickel with a sulfur containing compound.
摘要翻译：在一个实施方案中：在金属反应器中制备合成气的方法可以包括在催化剂存在下将二氧化碳和氢气导入金属反应器以形成合成气，其中金属反应器包含镍，其中二氧化碳和氢是与金属反应器的壁物理接触; 并用含硫化合物钝化镍。

38. 发明授权

US09447326B2 Pretreatment of biomass using steam explosion methods before gasification 有权
标题翻译：气化前采用蒸汽爆炸法预处理生物质
公开(公告)号：US09447326B2
公开(公告)日：2016-09-20
申请号：US14276719
申请日：2014-05-13
申请人： Sundrop Fuels, Inc.
发明人： Francis Michael Ferraro , Jerrod Wayne Hohman , Robert S. Ampulski
IPC分类号： B01J7/00 , C10B49/02 , C07C29/151 , C10J3/48 , C10K3/02 , C10L9/08 , D21C1/02 , B01J8/08 , B01J8/12 , B01J19/02 , B01J8/00 , C10G2/00
CPC分类号： C10B49/02 , B01J8/0025 , B01J8/087 , B01J8/12 , B01J19/02 , B01J2208/00123 , B01J2208/00132 , B01J2208/00504 , B01J2208/00513 , B01J2208/0084 , B01J2219/0263 , C07C29/1518 , C10G2/32 , C10G2300/1014 , C10J3/485 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/092 , C10J2300/0976 , C10J2300/1223 , C10J2300/1665 , C10J2300/1853 , C10K3/02 , C10L9/083 , D21C1/02 , Y02E50/15 , Y02E50/18 , Y02P20/145 , Y02P30/20 , C07C31/04
摘要： An integrated plant that includes a steam explosion process unit and biomass gasifier to generate syngas from biomass is discussed. A steam explosion process unit applies a combination of heat, pressure, and moisture to the biomass to make the biomass into a moist fine particle form. The steam explosion process unit applies steam with a high pressure to heat and pressurize any gases and fluids present inside the biomass to internally blow apart the bulk structure of the biomass via a rapid depressurization of the biomass with the increased moisture content. Those produced moist fine particles of biomass are subsequently fed to a feed section of the biomass gasifier, which reacts the biomass particles in a rapid biomass gasification reaction to produce syngas components.
摘要翻译：讨论了一个综合工厂，其中包括一个蒸汽爆炸处理装置和生物质气化器从生物质产生合成气。蒸汽爆炸处理单元将热量，压力和水分的组合应用于生物质，以使生物质成为潮湿的细颗粒形式。蒸汽爆炸过程单元应用高压蒸汽来对生物质内存在的任何气体和流体进行加压并对其进行加压，以通过具有增加的水分含量的生物质的快速减压来内部吹散生物质的本体结构。产生生物质的湿细颗粒的产物随后被送入生物质气化器的进料部分，其使生物质颗粒在快速的生物质气化反应中反应以产生合成气组分。

39. 发明授权

US09422494B2 Process for producing renewable jet fuel compositions 有权
标题翻译：生产可再生喷气燃料组合物的方法
公开(公告)号：US09422494B2
公开(公告)日：2016-08-23
申请号：US14323452
申请日：2014-07-03
申请人： David Bradin
发明人： David Bradin
IPC分类号： C07C1/04 , C07C1/12 , C07C1/207 , C07C1/24 , C07C2/06 , C07C5/02 , C07C5/22 , C10L1/04 , C07C41/09 , C10G50/00 , C07C29/151 , C10G69/12 , C10G3/00
CPC分类号： C10L1/04 , C07C1/24 , C07C29/1518 , C07C41/09 , C10G3/49 , C10G50/00 , C10G69/126 , C10G2300/1014 , C10G2400/08 , C10J2300/1665 , Y02E20/18 , Y02E50/18 , Y02P20/52 , C07C11/04 , C07C11/02 , C07C31/04 , C07C31/08 , C07C43/043
摘要： The present invention provides a process for producing jet fuel components from syngas. Syngas is converted to methanol and ethanol, and, optionally, higher alcohols. The methanol is separated from the ethanol and higher alcohols, and converted to C5-9 paraffins and aromatics via a dimethyl ether intermediate. The dimethyl ether is reacted over a catalyst to form jet fuel range hydrocarbons and aromatics. The ethanol and higher alcohols are dehydrated to form olefins, which are then oligomerized and, optionally, hydrogenated and/or isomerized, to form products in the jet fuel range. All or part of the two separate product streams can be combined, to provide jet fuel components which include aromatics and paraffins, ideally isoparaffins, in the jet fuel range. The syngas is in one embodiment derived from biomass or another renewable carbon-containing feedstock, thereby providing a biorefining process for producing renewable jet fuel.
摘要翻译：本发明提供从合成气生产喷气燃料成分的方法。将合成气转化为甲醇和乙醇，以及任选的高级醇。甲醇与乙醇和高级醇分离，并通过二甲醚中间体转化成C5-9链烷烃和芳族化合物。二甲醚在催化剂上反应形成喷气燃料范围的烃和芳族化合物。乙醇和高级醇被脱水以形成烯烃，然后将其低聚并任选地氢化和/或异构化以在喷气燃料范围内形成产物。可以组合两个分离的产物流中的全部或部分，以在喷气燃料范围内提供喷气燃料组分，其包括芳族化合物和石蜡，理想上是异链烷烃。在一个实施方案中，合成气衍生自生物质或另一种可再生碳的原料，从而提供用于生产可再生喷气燃料的生物精制方法。

40. 发明授权

US09394219B2 Method for producing synthesis gas for methanol production 有权
标题翻译：生产甲醇合成气的方法
公开(公告)号：US09394219B2
公开(公告)日：2016-07-19
申请号：US14354531
申请日：2012-10-25
申请人： STAMICARBON B.V.
发明人： Gaetano Iaquaniello , Barbara Cucchiella , Elena Antonetti
IPC分类号： C07C29/48 , C01B3/38 , C01B3/48 , C07C29/151 , C01B3/32
CPC分类号： C07C29/48 , C01B3/323 , C01B3/386 , C01B3/48 , C01B2203/0261 , C01B2203/0283 , C01B2203/043 , C01B2203/0475 , C01B2203/061 , C01B2203/1235 , C01B2203/1258 , C01B2203/142 , C07C29/1518 , C07C31/04
摘要： Method for producing synthesis gas for methanol production The present invention relates to a method for producing synthesis gas from a hydrocarbon containing feed, which synthesis gas is particularly suitable for subsequent use in methanol production. In this method, a hydrocarbon containing feed, particularly natural gas (100), is subjected to catalytic partial oxidation (CPO) (2), followed by the water gas shift (WGS) (4) reaction of a part of the reformed feed. At least part of the shifted feed is then subjected to hydrogen purification, preferably by pressure swing adsorption (PSA) (5) to obtain pure hydrogen (108), which hydrogen is subsequently combined with the remaining parts of the feeds to yield synthesis gas particularly suitable for methanol synthesis. The recombined stream preferably has an R ratio, being the molar ratio (H2−CO2)/(CO+CO2), in the range 1.9-2.2 and preferably about 2. The invention further relates to a method for producing methanol from a hydrocarbon containing feed, wherein first synthesis gas is obtained according to the method of the invention, which synthesis gas is further used to produce methanol.
摘要翻译：用于生产甲醇生产合成气的方法本发明涉及一种由含烃进料生产合成气的方法，该合成气特别适用于随后用于甲醇生产。在该方法中，将含烃进料，特别是天然气（100）进行催化部分氧化（CPO）（2），然后进行部分重整进料的水煤气变换（WGS）（4）反应。然后至少部分转移的进料进行氢气净化，优选通过变压吸附（PSA）（5）进行氢气净化，以获得纯氢气（108），该氢气随后与进料的剩余部分组合以产生合成气，特别是适合甲醇合成。重组流优选具有在1.9-2.2范围内，优选约2的摩尔比（H 2 -CO 2）/（CO + CO 2）的R比。本发明还涉及一种由含烃的进料，其中根据本发明的方法获得第一种合成气，该合成气被进一步用于生产甲醇。

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