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61. 发明申请

US20140200318A1 Methods for Production of Hydrocarbons and Oxygen-Containing Hyrdrocarbons 有权
标题翻译：碳氢化合物和含氧乙醛的生产方法
公开(公告)号：US20140200318A1
公开(公告)日：2014-07-17
申请号：US14117819
申请日：2012-05-16
申请人： The Regents of the University of California
发明人： Kenneth J. Shea , Jun Luo
IPC分类号： C08F4/08
CPC分类号： C08F4/08 , C08G61/04 , C08G2261/3326 , C10G1/002 , C10G2/00 , C10G3/00 , Y02P30/20
摘要： Environmentally friendly, energy efficient methods for making hydrocarbons, including oxygen containing hydrocarbons, linear or branched polymers, oligomers, waxes, small hydrocarbon molecules, fuels, coatings and starting materials/reactants to be used for making other hydrocarbons. A C1 carbon source, such as coal, natural gas, petroleum or biomass (including non-food biomass), is converted to the desired hydrocarbon. The reaction can be run in water, at room temperature and under atmospheric pressure. In some embodiments, the method comprises combining a) a C1 carbon source; b) water; c) an alkaline agent; and d) an alkyl Lewis acid in an amount effective to initiate or catalyze reaction of the components to form the hydrocarbon.
摘要翻译：用于制造碳氢化合物（包括含氧烃，直链或支链聚合物，低聚物，蜡，小烃分子，燃料，涂料和用于制备其它烃的原料/反应物）的环保节能方法。 C1碳源，如煤，天然气，石油或生物质（包括非食品生物质）等碳转化为所需的烃。该反应可以在水中，室温和大气压下进行。在一些实施方案中，该方法包括组合a）C1碳源; b）水; c）碱性试剂; 和d）有效引发或催化组分反应形成烃的烷基路易斯酸。

62. 发明申请

US20140183124A1 FILTER CLEANING APPARATUS 有权
标题翻译：过滤器清洗装置
公开(公告)号：US20140183124A1
公开(公告)日：2014-07-03
申请号：US14236669
申请日：2012-08-02
申请人： Atsushi Murata , Eiichi Yamada , Shinji Fukumoto
发明人： Atsushi Murata , Eiichi Yamada , Shinji Fukumoto
IPC分类号： B01D29/66
CPC分类号： B01D29/668 , B01D29/66 , B01D35/027 , B01D35/12 , C10G2/00 , C10G31/09 , C10G2300/1022
摘要： A filter cleaning apparatus used in a reaction system including; a reaction tank having a filter, first feed line connected to the filter at one end, a recovery tank connected to the other end of the first feed line, and second feed line connected to the recovery tank at one end, is provided. The filter cleaning apparatus includes; first return line connected the second feed line at one end, first and second reverse cleaning solution tanks connected to the first return line, a first flow rate adjusting valve that can adjust filtered fluid to be supplied to the first reverse cleaning solution tank, a second flow rate adjusting valve that can adjust filtered fluid to be supplied to the second reverse cleaning solution tank, and a switching section that carries either one of the filtered fluids accommodated in these reverse cleaning solution tanks by switching.
摘要翻译：一种用于反应系统的过滤器清洁装置，包括：具有过滤器的反应罐，一端连接到过滤器的第一供给管线，连接到第一供给管线的另一端的回收罐和在一端连接到回收罐的第二供给管线。过滤器清洁装置包括：第一回流管线连接在一端的第二进料管线，连接到第一回流管线的第一和第二反向清洗溶液罐，第一流量调节阀，其可以调节要供应到第一反向清洗溶液罐的过滤流体，第二回流管线流量调节阀，其可以调节要供给到第二反向清洗溶液箱的过滤流体;以及切换部，其通过切换运送容纳在这些反向清洗液罐中的一个过滤流体。

63. 发明申请

US20140100294A1 RENEWABLE ELECTRICITY CONVERSION OF LIQUID FUELS FROM HYDROCARBON FEEDSTOCKS 审中-公开
标题翻译：液化石油气可再生能源转换
公开(公告)号：US20140100294A1
公开(公告)日：2014-04-10
申请号：US14077094
申请日：2013-11-11
申请人： INENTEC INC.
发明人： Daniel R. Cohn , Jeffrey E. Surma , Leslie Bromberg
IPC分类号： C01B3/36 , C07C29/15 , C10G2/00
CPC分类号： C10G2/32 , C01B3/24 , C01B3/36 , C01B13/0229 , C01B2203/0216 , C01B2203/0255 , C01B2203/0272 , C01B2203/06 , C01B2203/061 , C01B2203/0833 , C01B2203/085 , C01B2203/0861 , C01B2203/0866 , C01B2203/1235 , C01B2203/1241 , C01B2203/82 , C01B2203/84 , C01B2203/86 , C07C29/15 , C07C29/151 , C10G2/00 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10J3/00 , C10J3/82 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/0959 , C10J2300/1284 , C10J2300/1659 , C10J2300/1665 , C10J2300/1684 , C10J2300/1846 , F23G5/46 , F23G2206/203 , Y02E20/12 , Y02E50/13 , Y02E50/18 , Y02E50/32 , Y02P20/133 , Y02P20/134 , Y02P20/145 , Y02P20/582 , Y02P30/10 , Y02P30/30 , Y02T50/678
摘要： The present invention includes a method for converting renewable energy source electricity and a hydrocarbon feedstock into a liquid fuel by providing a source of renewable electrical energy in communication with a synthesis gas generation unit and an air separation unit. Oxygen from the air separation unit and a hydrocarbon feedstock is provided to the synthesis gas generation unit, thereby causing partial oxidation reactions in the synthesis gas generation unit in a process that converts the hydrocarbon feedstock into synthesis gas. The synthesis gas is then converted into a liquid fuel.
摘要翻译：本发明包括通过提供与合成气生成单元和空气分离单元连通的可再生电能源将可再生能源电和烃原料转化为液体燃料的方法。在合成气产生单元中提供来自空气分离单元的氧气和烃原料，从而在将烃原料转化为合成气的过程中在合成气产生单元中引起部分氧化反应。然后将合成气转化为液体燃料。

64. 发明授权

US08614364B2 Renewable electricity conversion of liquid fuels from hydrocarbon feedstocks 有权
标题翻译：从碳氢化合物原料可再生能源转换液体燃料
公开(公告)号：US08614364B2
公开(公告)日：2013-12-24
申请号：US12575305
申请日：2009-10-07
申请人： Daniel R. Cohn , Jeffrey E. Surma , Leslie Bromberg
发明人： Daniel R. Cohn , Jeffrey E. Surma , Leslie Bromberg
IPC分类号： C07C1/00
CPC分类号： C10G2/32 , C01B3/24 , C01B3/36 , C01B13/0229 , C01B2203/0216 , C01B2203/0255 , C01B2203/0272 , C01B2203/06 , C01B2203/061 , C01B2203/0833 , C01B2203/085 , C01B2203/0861 , C01B2203/0866 , C01B2203/1235 , C01B2203/1241 , C01B2203/82 , C01B2203/84 , C01B2203/86 , C07C29/15 , C07C29/151 , C10G2/00 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10J3/00 , C10J3/82 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/0959 , C10J2300/1284 , C10J2300/1659 , C10J2300/1665 , C10J2300/1684 , C10J2300/1846 , F23G5/46 , F23G2206/203 , Y02E20/12 , Y02E50/13 , Y02E50/18 , Y02E50/32 , Y02P20/133 , Y02P20/134 , Y02P20/145 , Y02P20/582 , Y02P30/10 , Y02P30/30 , Y02T50/678
摘要： A method for converting renewable energy source electricity and a hydrocarbon feedstock into a liquid fuel by providing a source of renewable electrical energy in communication with a synthesis gas generation unit and an air separation unit is described. Oxygen from the air separation unit and a hydrocarbon feedstock is provided to the synthesis gas generation unit, thereby causing partial oxidation reactions in the synthesis gas generation unit in a process that converts the hydrocarbon feedstock into synthesis gas. The synthesis gas is then converted into a liquid fuel.
摘要翻译：描述了通过提供与合成气产生单元和空气分离单元连通的可再生电能源将可再生能源电和烃原料转化为液体燃料的方法。在合成气产生单元中提供来自空气分离单元的氧气和烃原料，从而在将烃原料转化为合成气的过程中在合成气产生单元中引起部分氧化反应。然后将合成气转化为液体燃料。

65. 发明申请

US20130144099A1 METHOD FOR PRODUCING HYDROCARBON OIL AND SYSTEM FOR PRODUCING HYDROCARBON OIL 有权
标题翻译：生产烃油的方法和生产烃油的方法
公开(公告)号：US20130144099A1
公开(公告)日：2013-06-06
申请号：US13817182
申请日：2011-08-12
申请人： Kazuhiko Tasaka , Yuichi Tanaka , Marie Iwama
发明人： Kazuhiko Tasaka , Yuichi Tanaka , Marie Iwama
IPC分类号： C10G67/00
CPC分类号： C10G67/02 , C10G2/00 , C10G2/342 , C10G3/56 , C10G31/00 , C10G47/00 , C10G65/18 , C10G67/00 , C10G67/16 , C10G2300/1022 , C10G2300/208 , Y02P30/20
摘要： Hydrocarbon oil obtained by Fischer-Tropsch (FT) synthesis reaction using a catalyst within a slurry bed reactor is fractionated into a distilled oil and a column bottom oil in a rectifying column, part of the column bottom oil is flowed into a first transfer line that connects a column bottom of the rectifying column to a hydrocracker, at least part of the column bottom oil is flowed into a second transfer line branched from the first transfer line and connected to the first transfer line downstream of the branching point, the amount of the catalyst fine powder to be captured is monitored while the catalyst fine powder in the column bottom oil that flows in the second transfer line are captured by a detachable filter provided in the second transfer line, and the column bottom oil is hydrocracked within the hydrocracker.
摘要翻译：通过使用在淤浆床反应器内的催化剂的费 - 托（FT）合成反应获得的烃油被分馏成精馏塔中的蒸馏油和塔底油，部分塔底油流入第一输送管线，将精馏塔的塔底连接到加氢裂化器，至少部分塔底油流入从第一输送管线分支并与分支点下游的第一输送管线连接的第二输送管线，监测待捕获的催化剂细粉末，同时通过设置在第二输送管线中的可拆卸过滤器捕集在第二输送管线中流动的塔底油中的催化剂细粉末，并将塔底油在加氢裂化器内加氢裂化。

66. 发明授权

US08435457B2 Synthesis of hydrocarbons via catalytic reduction of CO2 有权
标题翻译：通过CO 2的催化还原合成烃
公开(公告)号：US08435457B2
公开(公告)日：2013-05-07
申请号：US13181566
申请日：2011-07-13
申请人： Nick E Tran , Dennis R Hardy , Samuel G Lambrakos , John G. Michopoulos
发明人： Nick E Tran , Dennis R Hardy , Samuel G Lambrakos , John G. Michopoulos
IPC分类号： B01J8/02 , B01J19/00
CPC分类号： C10G2/50 , B01J8/0285 , B01J8/067 , B01J2208/00044 , B01J2208/0007 , B01J2208/00176 , C01B3/042 , C01B2203/062 , C10G2/00 , C10G2/32 , C10G2/332 , C10G2/334 , Y02E60/364 , Y02P20/142
摘要： A method of: introducing hydrogen and a feed gas containing at least 50 vol % carbon dioxide into a reactor containing a Fischer-Tropsch catalyst; and heating the hydrogen and carbon dioxide to a temperature of at least about 190° C. to produce hydrocarbons in the reactor. An apparatus having: a reaction vessel for containing a Fischer-Tropsch catalyst, capable of heating gases to at least about 190° C.; a hydrogen delivery system feeding into the reaction vessel; a carbon dioxide delivery system for delivering a feed gas containing at least 50 vol % carbon dioxide feeding into the reaction vessel; and a trap for collecting hydrocarbons generated in the reaction vessel.
摘要翻译：一种将含有至少50体积％二氧化碳的氢气和进料气体引入含有费 - 托催化剂的反应器中的方法; 并将氢气和二氧化碳加热到至少约190℃的温度以在反应器中产生烃。一种装置，具有：用于容纳费 - 托催化剂的反应容器，其能够将气体加热至至少约190℃; 供给到反应容器中的氢输送系统; 用于将含有至少50体积％二氧化碳的进料气体输送到反应容器中的二氧化碳输送系统; 以及用于收集在反应容器中产生的烃的捕集阱。

67. 发明申请

US20120315215A1 METHOD OF HYDROCARBONS AND HYDROGEN PRODUCTION FROM WATER AND CARBON DIOXIDE 有权
标题翻译：水和二氧化碳的氢生产方法
公开(公告)号：US20120315215A1
公开(公告)日：2012-12-13
申请号：US13578222
申请日：2011-12-26
申请人： Azary Aleksandrovich Barenbaum , Sumbat Nabievich Zakirov , Ernest Sumbatovich Zakirov , Vladimir Aleksandrovich Serebryakov
发明人： Azary Aleksandrovich Barenbaum , Sumbat Nabievich Zakirov , Ernest Sumbatovich Zakirov , Vladimir Aleksandrovich Serebryakov
IPC分类号： C01B3/04 , C01B13/02 , C07C1/02
CPC分类号： C10G2/50 , C01B3/06 , C01B13/0207 , C10G2/00 , C10G2300/805 , Y02E60/36
摘要： The disclosure relates to energy and the production of cost-effective power sources as hydrocarbons and hydrogen, as well as an oxidizer, such as oxygen. In an embodiment, the method of hydrocarbons, hydrogen and oxygen production includes a number of stages, including water saturation with carbon dioxide to form a saturated carbonated water; passing of the carbonated water through the reactor, which contains a catalyst, with the formation of hydrocarbons, hydrogen and oxygen, that subsequently flow into a separator; separation of reaction products from the initial carbonated water in the separator by liquid and gaseous phase separation, while hydrocarbons are separated from the liquid and gaseous phases, and hydrogen and oxygen are additionally separated from the gaseous phase.
摘要翻译：本公开涉及能量和生产作为碳氢化合物和氢的成本有效的电源，以及氧化剂，例如氧气。在一个实施方案中，烃，氢和氧产生的方法包括许多阶段，包括与二氧化碳的水饱和以形成饱和碳酸水; 使碳酸水通过含有催化剂的反应器，形成烃，氢和氧，随后流入分离器; 通过液相和气相分离将反应产物与分离器中的初始碳酸水分离，同时将烃与液相和气相分离，并将氢气和氧气从气相中分离出来。

68. 发明申请

US20120291341A1 How to produce synthetic gasolines or synthetic diesels using only natural gas as raw material. 有权
标题翻译：如何生产仅使用天然气为原料的合成汽油或合成柴油。
公开(公告)号：US20120291341A1
公开(公告)日：2012-11-22
申请号：US13068624
申请日：2011-05-17
申请人： Robert Gagnon
发明人： Robert Gagnon
IPC分类号： C10L1/12 , C01B3/36
CPC分类号： C10G3/45 , C01B3/36 , C01B2203/025 , C10G2/00 , C10G2300/1025 , C10G2300/4006 , C10G2300/4012 , C10G2400/02 , C10G2400/04 , Y02P30/20
摘要： My process does not convert natural gas into compressed natural gas, does not convert natural gas into liquified natural gas but uses 2 new chemical formulas to convert natural gas into synthetic gasolines or into synthetic diesels. After producing CO through a technology of partial combustion , my process improves Fischer-Tropsch process using CH4 instead of H2, following 2 new chemical equations and adding salt, NaCl, to an iron, FeO, catalyst or to any other catalyst capable of generating hydrocarbons. Instead of producing a large variety of synthetic hydrocarbons like other processes do, my process delivers only synthetic gasolines following 5 CH4+2 CO=C7H16+2 H2O or only synthetic diesels following 11 CH4+5 CO=C16H34+5 H2O thanks to the addition of salt to an iron catalyst or to any other catalyst. No oil refining needed. Because natural gas is the cleanest hydrocarbon, my process produces clean synthetic gasolines or clean synthetic diesels. Because the prices of natural gas are very low, my process produces clean synthetic gasolines or clean synthetic diesels at very low costs.
摘要翻译：我的过程不会将天然气转化为压缩天然气，不会将天然气转化为液化天然气，而是使用两种新的化学配方将天然气转化为合成汽油或合成柴油。在通过部分燃烧技术生产CO后，我的工艺改进了使用CH4而不是H2的费 - 托工艺，遵循2个新的化学方程，并向铁，FeO，催化剂或能够产生碳氢化合物的任何其他催化剂中加入盐，NaCl 。不像其他工艺那样生产各种各样的合成烃，我的工艺只能在5 CH4 + 2CO = C7H16 + 2H2O之后提供合成的汽油，或仅在11 CH4 + 5CO = C16H34 + 5H2O之后合成柴油，因为加入的盐与铁催化剂或任何其它催化剂反应。不需要炼油。由于天然气是最干净的碳氢化合物，我的工艺生产清洁的合成汽油或清洁的合成柴油。由于天然气价格非常低，我的工艺以非常低的成本生产清洁的合成汽油或清洁的合成柴油。

69. 发明申请

US20120184633A1 MICROCHANNEL COMPRESSION REACTOR 有权
标题翻译：微通道压缩反应器
公开(公告)号：US20120184633A1
公开(公告)日：2012-07-19
申请号：US13427647
申请日：2012-03-22
申请人： William Allen Rogers , Paul William NEAGLE , Michael Alan MARCHlANDO , Christopher Paul Weil , Robert Dwayne Litt , Ronald Chester Pasadyn , G. Bradley Smith , Charles Robert Miele , Thomas Peter Forte , Jimmy Glen Pelham
发明人： William Allen Rogers , Paul William NEAGLE , Michael Alan MARCHlANDO , Christopher Paul Weil , Robert Dwayne Litt , Ronald Chester Pasadyn , G. Bradley Smith , Charles Robert Miele , Thomas Peter Forte , Jimmy Glen Pelham
IPC分类号： C07C1/04 , B23P6/00 , C01B3/38
CPC分类号： B01J19/0093 , B01J3/046 , B01J2219/0081 , B01J2219/00817 , B01J2219/00835 , B01J2219/00867 , B01J2219/00869 , B01J2219/00873 , B01J2219/00891 , B01J2219/00957 , B01J2219/00961 , B01J2219/00963 , B01J2219/00986 , C01B3/382 , C01B3/384 , C01B2203/0227 , C01B2203/0283 , C01B2203/0811 , C01B2203/1604 , C07C1/0475 , C07C1/0485 , C10G2/00 , C10G2300/4031 , Y02P20/52 , Y10T29/49345 , Y10T29/49815 , Y10T29/49826 , Y10T29/49948 , Y10T137/0335
摘要： The present invention includes a removable microchannel unit including an inlet orifice and an outlet orifice in fluid communication with a plurality of microchannels distributed throughout the removable microchannel unit, and a pressurized vessel adapted have the removable microchannel unit mounted thereto, the pressurized vessel adapted to contain a pressurized fluid exerting a positive gauge pressure upon at least a portion of the exterior of the removable microchannel unit. The invention also includes a microchannel unit assembly comprising a microchannel unit operation carried out within a pressurized vessel, where pressurized vessel includes a pressurized fluid exerting a positive gauge pressure upon an exterior of the microchannel unit operation, and where the microchannel unit operation includes an outlet orifice in fluid communication with an interior of the pressurized vessel.
摘要翻译：本发明包括可拆卸微通道单元，其包括入口孔和与遍布可移除微通道单元分布的多个微通道流体连通的出口孔，以及适于具有安装在其上的可移除微通道单元的加压容器，该加压容器适于容纳加压流体在可移除的微通道单元的外部的至少一部分上施加正的表压。本发明还包括微通道单元组件，其包括在加压容器内执行的微通道单元操作，其中加压容器包括在微通道单元操作的外部施加正表压的加压流体，并且其中微通道单元操作包括出口孔与压力容器的内部流体连通。

70. 发明申请

US20110268617A1 SYNTHESIS OF HYDROCARBONS VIA CATALYTIC REDUCTION OF CO2 有权
标题翻译：通过二氧化碳的催化还原来合成碳氢化合物
公开(公告)号：US20110268617A1
公开(公告)日：2011-11-03
申请号：US13181566
申请日：2011-07-13
申请人： Nick E. Tran , Dennis R. Hardy , Samuel G. Lambrakos , John G. Michopoulos
发明人： Nick E. Tran , Dennis R. Hardy , Samuel G. Lambrakos , John G. Michopoulos
IPC分类号： B01J19/00
CPC分类号： C10G2/50 , B01J8/0285 , B01J8/067 , B01J2208/00044 , B01J2208/0007 , B01J2208/00176 , C01B3/042 , C01B2203/062 , C10G2/00 , C10G2/32 , C10G2/332 , C10G2/334 , Y02E60/364 , Y02P20/142
摘要： A method of: introducing hydrogen and a feed gas containing at least 50 vol % carbon dioxide into a reactor containing a Fischer-Tropsch catalyst; and heating the hydrogen and carbon dioxide to a temperature of at least about 190° C. to produce hydrocarbons in the reactor. An apparatus having: a reaction vessel for containing a Fischer-Tropsch catalyst, capable of heating gases to at least about 190° C.; a hydrogen delivery system feeding into the reaction vessel; a carbon dioxide delivery system for delivering a feed gas containing at least 50 vol % carbon dioxide feeding into the reaction vessel; and a trap for collecting hydrocarbons generated in the reaction vessel.
摘要翻译：一种将含有至少50体积％二氧化碳的氢气和进料气体引入含有费 - 托催化剂的反应器中的方法; 并将氢气和二氧化碳加热到至少约190℃的温度以在反应器中产生烃。一种装置，具有：用于容纳费 - 托催化剂的反应容器，其能够将气体加热至至少约190℃; 供给到反应容器中的氢输送系统; 用于将含有至少50体积％二氧化碳的进料气体输送到反应容器中的二氧化碳输送系统; 以及用于收集在反应容器中产生的烃的捕集阱。

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