公开(公告)号：US20240110112A1

公开(公告)日：2024-04-04

申请号：US18479120

申请日：2023-10-02

Applicant: HONDA MOTOR CO., LTD.

Inventor： Hiroshi CHISHIMA ,  Kohtaro HASHIMOTO

IPC: C10J3/72 ,  C10L1/04

CPC classification number: C10J3/723 ,  C10L1/04 ,  C10J2200/15 ,  C10J2300/0916 ,  C10J2300/1656 ,  C10J2300/1684

Abstract: A fuel production system and a fuel production method are provided which can efficiently perform adjusting of a synthesis gas composition by hydrogen supply, while suppressing the generated amount of carbon dioxide by a system overall. A fuel production system includes: a gasification furnace which gasifies a biomass raw material to generate a synthesis gas containing hydrogen and carbon monoxide; a liquid fuel production device which produces a liquid fuel from the synthesis gas generated by the gasification furnace; a hydrogen supply pump which supplies hydrogen to a raw material supply area or a synthesis gas discharge area; a temperature sensor which detects a temperature of the gasification furnace; and a controller which switches a hydrogen supply location by the hydrogen supply pump between the raw material supply area and synthesis gas discharge area, based on the temperature detected by the temperature sensor.

公开(公告)号：US20180258847A1

公开(公告)日：2018-09-13

申请号：US15973674

申请日：2018-05-08

Applicant: Karl Werner DIETRICH

Inventor： Karl Werner DIETRICH

IPC: F02C3/22 ,  C25B1/04 ,  C10L3/10 ,  C10J3/00 ,  C07C1/12

CPC classification number: F02C3/22 ,  C07C1/12 ,  C10J3/00 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/1612 ,  C10J2300/1662 ,  C10J2300/1684 ,  C10L3/10 ,  C25B1/04 ,  Y02E60/366 ,  Y02P20/133 ,  Y02P20/134

Abstract: According to known methods, biomass is broken down under the action of water vapour via a carbon monoxide-hydrogen mixture (called synthesis gas) as an intermediate stage into hydrogen and carbon dioxide instead of being combusted directly to generate energy. Carbon dioxide is stored/sequestered and the hydrogen is used to generate energy. The transfer of bio-activity can also be effected within the same process by breaking down a mixture of biomass and fossil fuel (e.g. wood and coal) into carbon dioxide and hydrogen. The hydrogen is then reacted with half of the formed carbon dioxide to form methane and the remaining carbon dioxide is stored. The stored carbon dioxide and generated methane respectively comprise one half each of biological and fossil carbon. If the bio-activity of the stored biocarbon dioxide is transferred to the fossil carbon in methane, a corresponding mixture of wood and coal produces 100% biomethane. Here, too, up to 100% biomethane can be obtained from coal-wood mixtures. By adding the hydrogen obtained from excess electrical energy to the biocarbon, the bio-energy based on the biomass used is even quadrupled. For a traceable eco-balance with such mixtures, it is important to quantify the bio-proportion in the two “end products” stored carbon dioxide and generated methane. For this purpose, use is made e.g. of the radiocarbon (C14) method.

公开(公告)号：US09496565B2

公开(公告)日：2016-11-15

申请号：US12526008

申请日：2008-02-06

Applicant: Reinder J. Boersma ,  Scott C. Rackey ,  Jack A. Shindle

Inventor： Reinder J. Boersma ,  Scott C. Rackey ,  Jack A. Shindle

IPC: H01M8/06 ,  C25B1/02 ,  B01J8/00 ,  C01B3/02 ,  H01M8/04 ,  C01B3/34 ,  C01B3/36 ,  C01B3/38 ,  C10J3/00

CPC classification number: H01M8/04014 ,  C01B3/34 ,  C01B3/36 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/04 ,  C01B2203/06 ,  C01B2203/0883 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/142 ,  C01B2203/84 ,  C10J3/00 ,  C10J2300/1646 ,  C10J2300/1684 ,  H01M8/04089 ,  H01M8/04119 ,  H01M8/04291 ,  H01M8/0612 ,  H01M8/0618 ,  H01M8/0631 ,  H01M8/0656 ,  H01M8/0662 ,  H01M8/0668 ,  Y02E60/364 ,  Y02E60/50

Abstract: The present invention generally relates to electrochemical systems for producing hydrogen and/or power. Various aspects of the invention are directed to reactor designs for producing hydrogen and/or power from a fuel and water, conducting ceramics and other materials for such systems, including mixed ionically and electrically conducting ceramics which can be used for hydrogen gas generation, control systems for such systems, and methods of operating such systems.

Abstract translation: 本发明一般涉及用于产生氢和/或电力的电化学系统。 本发明的各个方面涉及从燃料和水生产氢和/或电力的反应器设计，用于这种系统的导电陶瓷和其它材料，包括可用于氢气产生的混合离子和导电陶瓷，控制系统 对于这样的系统，以及操作这种系统的方法。

公开(公告)号：US09469533B2

公开(公告)日：2016-10-18

申请号：US14077094

申请日：2013-11-11

Applicant: INENTEC INC.

Inventor： Daniel R. Cohn ,  Jeffrey E. Surma ,  Leslie Bromberg

IPC: C07C1/00 ,  C01B3/36 ,  C01B3/24 ,  C10G2/00 ,  C10J3/00 ,  F23G5/46 ,  C07C29/15

CPC classification number: 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

Abstract: 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.

Abstract translation: 一种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。 向合成气生成单元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体发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。

公开(公告)号：US09328426B2

公开(公告)日：2016-05-03

申请号：US13430590

申请日：2012-03-26

Applicant: Judith Pauline Oppenheim

Inventor： Judith Pauline Oppenheim

IPC: C25B1/04 ,  C25B15/00 ,  C25B15/02 ,  C25B9/00 ,  F02B43/08 ,  F23N1/02 ,  H01M8/06 ,  F22B1/00 ,  F24J2/07 ,  C10K1/00 ,  F24J2/00

CPC classification number: C25B1/04 ,  C10J2300/0959 ,  C10J2300/0966 ,  C10J2300/1653 ,  C10J2300/1684 ,  C10K1/003 ,  C25B15/00 ,  F22B1/006 ,  F24S20/20 ,  F24S2020/17 ,  Y02E10/41 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E60/366 ,  Y02E70/10

Abstract: A system includes a photoelectrolysis system having a solar collector configured to collect and concentrate solar radiation to heat water, generate electricity, or both. The system also includes an electrolysis unit configured to electrolyze the heated water using at least the generated electricity to produce a first gas mixture and a second gas mixture. The first gas mixture includes oxygen and steam and the second gas mixture includes hydrogen and steam. The system further includes a first device configured to receive and use the first gas mixture as well as a hydrogen membrane configured to receive and separate the hydrogen and steam mixture into a hydrogen component and a steam component.

Abstract translation: 一种系统包括光电解系统，其具有被配置为收集和集中太阳辐射以加热水，发电或两者的太阳能收集器。 该系统还包括电解单元，其被配置为使用至少所产生的电来对加热的水进行电解以产生第一气体混合物和第二气体混合物。 第一气体混合物包括氧气和蒸汽，第二气体混合物包括氢气和蒸汽。 该系统还包括被配置为接收和使用第一气体混合物的第一装置以及被配置为将氢气和蒸汽混合物接收并分离成氢组分和蒸汽组分的氢膜。

公开(公告)号：US20130137783A1

公开(公告)日：2013-05-30

申请号：US13510729

申请日：2010-11-22

Applicant: Challapalli Naga Kiran Kumar ,  Kim-Chinh Tran ,  Omar Freyr Sigurbjornsson ,  Jonathan Whitlow ,  Kathleen Alexander

Inventor： Challapalli Naga Kiran Kumar ,  Kim-Chinh Tran ,  Omar Freyr Sigurbjornsson ,  Jonathan Whitlow ,  Kathleen Alexander

IPC: C07C27/04 ,  C07C1/02 ,  C10J3/00

CPC classification number: C07C1/02 ,  C01B3/02 ,  C01B3/36 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/06 ,  C01B2203/1241 ,  C01B2203/84 ,  C10G2/00 ,  C10G2/32 ,  C10G2300/1003 ,  C10G2300/1014 ,  C10G2300/4043 ,  C10J3/00 ,  C10J2300/0916 ,  C10J2300/0959 ,  C10J2300/0966 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1284 ,  C10J2300/1612 ,  C10J2300/1643 ,  C10J2300/1646 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1693 ,  C10J2300/1815 ,  C10J2300/1823 ,  C10K1/005 ,  C10K3/06 ,  C25B1/04 ,  C25B15/08 ,  Y02E10/725 ,  Y02E20/16 ,  Y02E50/18 ,  Y02E50/32 ,  Y02E60/364 ,  Y02E60/366 ,  Y02E70/10 ,  Y02P20/133 ,  Y02P20/145 ,  Y02P30/10 ,  Y02P30/20 ,  Y02P30/446

Abstract: A method and system for converting intermittent renewable energy and renewable carbonaceous feedstock to non-intermittent renewable electrical and thermal energy, storing it as fuels and chemicals and using it to capture and re-use or dispose of CO2 emissions. The system in a preferred embodiment is realized through the generation of non-intermittent renewable electricity utilizing intermittent renewable energy sources along with gaseous fuel from renewable carbonaceous feedstock, producing oxygen and hydrogen from non-intermittent renewable electricity and utilizing the oxygen and hydrogen as required for gasification of renewable carbonaceous feedstock to produce gaseous fuel stream and gaseous intermediate stream, utilizing the gaseous intermediate stream to produce renewable fuels and renewable chemicals, and utilizing oxygen for oxy-rich combustion for concentrating CO2 emissions for easy processing, re-use and disposal.

Abstract translation: 将间歇式可再生能源和可再生碳质原料转化为非间歇性可再生电力和热能的方法和系统，将其储存为燃料和化学品，并将其用于捕获和再利用或处置二氧化碳排放。 优选实施例中的系统通过利用间歇式可再生能源以及来自可再生碳质原料的气体燃料产生非间歇性可再生电力来实现，从非间歇可再生电力产生氧气和氢气，并根据需要使用氧气和氢气 将可再生碳质原料气化以产生气态燃料流和气态中间物流，利用气态中间料流生产可再生燃料和可再生化学品，并利用氧气进行富氧燃烧，用于浓缩二氧化碳排放，以便于处理，再利用和处理。

公开(公告)号：US20110185634A1

公开(公告)日：2011-08-04

申请号：US12991219

申请日：2009-03-11

Applicant: Michael Prestel

Inventor： Michael Prestel

IPC: C10J3/46 ,  B01J19/08 ,  C07C35/00

CPC classification number: C10J3/18 ,  C07C29/1518 ,  C10J3/04 ,  C10J3/06 ,  C10J3/66 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/0966 ,  C10J2300/0969 ,  C10J2300/1276 ,  C10J2300/1284 ,  C10J2300/1646 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1807 ,  C10J2300/1823 ,  C10J2300/1853 ,  C10K1/08 ,  C10K1/122 ,  C10K3/001 ,  C10K3/006 ,  C10K3/023 ,  C10K3/04 ,  Y02E20/18 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/129 ,  Y02P20/145 ,  C07C31/04

Abstract: A device for extracting fuels from biomass while adding electrical energy, comprising a gasifier for gasifying the biomass while adding electrical energy to a gas mixture, a reformer for reforming the gas mixture obtained from the gasification, a gas scrubber for scrubbing the reformed gas mixture, a catalyst for carrying out a catalytic reaction for obtaining a reaction mixture from the scrubbed gas mixture, and a separator for separating the fuel from the reaction mixture, the device further comprising devices for supplying hydrogen for hydrogenating the biomass or the gas mixture obtained from gasification and representing a closed system having a uniform internal pressure in an operating state.

Abstract translation: 一种用于在添加电能的同时从生物质中提取燃料的装置，包括用于气化生物质的气化器，同时向气体混合物中加入电能，用于重整从气化获得的气体混合物的重整器，用于洗涤重整气体混合物的气体洗涤器， 用于进行催化反应以从洗涤的气体混合物获得反应混合物的催化剂和用于从反应混合物中分离燃料的分离器，该装置还包括用于供应氢气以氢化生物质或从气化获得的气体混合物的装置 并且表示在操作状态下具有均匀内部压力的封闭系统。

公开(公告)号：US20110065815A1

公开(公告)日：2011-03-17

申请号：US12673771

申请日：2008-08-13

Applicant: Masayasu Sakai ,  Tadashi Yokoi

Inventor： Masayasu Sakai ,  Tadashi Yokoi

IPC: C07C27/06 ,  B01J19/00

CPC classification number: C10J3/20 ,  B01J21/08 ,  B01J23/75 ,  C10G2/32 ,  C10J3/34 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/0973 ,  C10J2300/1246 ,  C10J2300/1606 ,  C10J2300/1659 ,  C10J2300/1684 ,  C10J2300/1693 ,  C10J2300/1853 ,  C10J2300/1876 ,  Y02E50/32 ,  Y02P20/133 ,  Y02P20/145 ,  Y02P20/52

Abstract: Disclosed is an apparatus for producing a hydrocarbon from a biomass such as a glass or wood, which comprises: a biomass gasification unit (101) for feeding a raw material biomass (MB) and an overheated water vapor (S) for gasifying the biomass and a fuel biomass (FB) and air (A) for burning the fuel biomass, thereby producing a mixed gas (G) mainly composed of hydrogen and carbon monoxide; a clean-up means (201) for purifying the mixed gas (G); a gas tank (301) for storing the cleaned-up mixed gas (G) temporarily; a pressurizing pump (401) for pressurizing the mixed gas (G); and a hydrocarbon synthesis unit (501) for converting the pressurized mixed gas (G) into a hydrocarbon.

Abstract translation: 公开了一种用于从诸如玻璃或木材的生物质生产烃的设备，其包括：用于供给原料生物质（MB）的生物质气化单元（101）和用于气化生物质的过热水蒸汽（S） 用于燃烧燃料生物质的燃料生物质（FB）和空气（A），从而产生主要由氢气和一氧化碳组成的混合气体（G）; 用于净化混合气体（G）的净化装置（201）; 用于临时存储净化的混合气体（G）的气罐（301） 用于对混合气体（G）加压的加压泵（401） 和用于将加压混合气体（G）转化成烃的烃合成装置（501）。

公开(公告)号：US07833296B2

公开(公告)日：2010-11-16

申请号：US11865649

申请日：2007-10-01

Applicant: Steve L. Clark

Inventor： Steve L. Clark

IPC: B01J7/00 ,  C01B3/24 ,  C01J3/46

CPC classification number: C10J3/00 ,  C10J2300/0959 ,  C10J2300/0963 ,  C10J2300/1238 ,  C10J2300/1606 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1684 ,  C10J2300/1807 ,  C10J2300/1823

Abstract: A system and process for maximizing the generation of electrical power from a variety of hydrocarbon feedstocks. The hydrocarbon feedstocks are first gasified and then oxidized in a two-chamber system and process using oxygen gas rather than ambient air. Intermediate gases generated in the system and process are recirculated and recycled to the gasification and oxidation chambers in order to maximize energy production. The energy produced through the system and process is used to generate steam and produce power through conventional steam turbine technology. In addition to the release of heat energy, the hydrocarbon feedstocks are oxidized to the pure product compounds of water and carbon dioxide, which are subsequently purified and marketed. The system and process minimizes environmental emissions.

Abstract translation: 用于最大化来自各种烃原料的电力产生的系统和方法。 烃原料首先气化，然后在双室系统中氧化，并使用氧气而不是环境空气进行氧化。 在系统和过程中产生的中间气体被再循环并再循环到气化和氧化室，以便最大限度地发电。 通过系统和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，烃原料被氧化成水和二氧化碳的纯产物化合物，随后进行纯化和上市。 系统和过程最大限度地减少了环境排放。

公开(公告)号：US07601524B1

公开(公告)日：2009-10-13

申请号：US11613045

申请日：2006-12-19

Applicant: Gary F. Seymour

Inventor： Gary F. Seymour

IPC: C12P7/14 ,  C10L1/182

CPC classification number: C10J3/00 ,  C10J2300/0916 ,  C10J2300/1284 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1684 ,  C10J2300/1876 ,  C10K1/101 ,  Y02E50/18 ,  Y02P20/128 ,  Y02P20/133 ,  Y02P20/134 ,  Y02P20/145

Abstract: A commercial production of synthetic fuel from bio-diesel by products system for efficiently producing synthetic fuels and other usable by-products. The composition includes providing glycerol, providing a first fermentation tank including a glycerol kinase substance, supplying the glycerol to the first fermentation tank, producing a phosphoenolpyruvate compound within the first fermentation tank, providing a second fermentation tank including a glycerol dehydrogenase substance, supplying the phosphoenolpyruvate compound to the second fermentation tank, producing a pyruvate compound within the second fermentation tank, providing a third fermentation tank including a pyruvate decarboxylase substance, supplying the pyruvate compound to the third fermentation tank, producing an acetaldehyde compound within the third fermentation tank, providing a fourth fermentation tank including an alcohol dehydrogenase substance, supplying the acetaldehyde compound to the fourth fermentation tank, producing ethanol within the fourth fermentation tank and collecting the ethanol produced by the fourth fermentation tank.

Abstract translation: 生物柴油合成燃料的商业生产按产品系统有效生产合成燃料和其他可用的副产物。 该组合物包括提供甘油，提供包含甘油激酶物质的第一发酵罐，向第一发酵罐供应甘油，在第一发酵罐内产生磷酸烯醇丙酮酸化合物，提供包含甘油脱氢酶物质的第二发酵罐，供应磷酸烯醇丙酮酸 与第二发酵罐混合，在第二发酵罐内产生丙酮酸盐化合物，提供包含丙酮酸脱羧酶物质的第三发酵罐，向第三发酵罐供应丙酮酸盐化合物，在第三发酵罐内产生乙醛化合物， 第四发酵罐，其包括醇脱氢酶物质，将乙醛化合物供应到第四发酵罐，在第四发酵罐内生产乙醇并收集由第四发酵罐产生的乙醇。