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31. 发明申请

WO2015144459A1 METHOD AND APPARATUS FOR CONVERSION OF LIQUID FUELS IN A REACTOR, USE OF AN APPARATUS FOR CONVERSION OF LIQUID FUELS 审中-公开
标题翻译：用于在反应器中转化液体燃料的方法和装置，使用用于液体燃料转化的装置
公开(公告)号：WO2015144459A1
公开(公告)日：2015-10-01
申请号：PCT/EP2015/055303
申请日：2015-03-13
申请人： CLEAN FUELS B.V.
发明人： SIEMONS, Roland
IPC分类号： B01J19/26 , B01J4/00 , F23D7/00 , F23D9/00
CPC分类号： B01J4/002 , B01J19/0026 , B01J2219/00247 , C01B3/02 , C01B3/22 , C01B2203/0266 , C01B2203/0272 , C10J3/48 , C10J3/485 , C10J2200/152 , C10J2300/0916 , C10J2300/0956 , C10J2300/0976 , C10J2300/1637 , F23D7/00 , F23D9/00 , F23D2900/00016
摘要： In an apparatus comprising a chamber (3) of a reactor drops (8) of a to be converted liquid are generated by a nozzle (2) positioned in a space (7) separate from the chamber (3). The drops (8) make a free fall thought the space 7 and enter via an opening (7a) the chamber (3) where they fall onto an evaporator body (9) for evaporation, the evaporated liquid leaves a solid deposit (1), A gaseous reactant line (11) supplies a reactant gas for conversion of the solid deposit (1) on the surface of the evaporator body.
摘要翻译：在包括反应器液滴（8）的室（3）的设备中，所述反应器液滴（8）由位于与所述室（3）分离的空间（7）中的喷嘴（2）产生。液滴（8）自由下落，认为空间7经由腔室（7a）进入腔室（3），在那里它们落在蒸发器主体（9）上用于蒸发，蒸发的液体留下固体沉积物（1），气态反应物管线（11）提供用于将固体沉积物（1）转化成蒸发器主体表面的反应气体。

32. 发明申请

WO2015041555A1 PROCESS AND INSTALLATION FOR PRODUCTION OF SYNTHESIS GAS 审中-公开
标题翻译：生产合成气的工艺和安装
公开(公告)号：WO2015041555A1
公开(公告)日：2015-03-26
申请号：PCT/RO2014/000026
申请日：2014-09-22
申请人： CELAC, Vasile
发明人： CELAC, Vasile
IPC分类号： C01B3/24 , C01B3/34 , B01J19/24
CPC分类号： C01B3/24 , B01J19/243 , B01J2219/0009 , B01J2219/00092 , B01J2219/00099 , B01J2219/00108 , B01J2219/00157 , C01B3/34 , C01B2203/0216 , C01B2203/0272 , C01B2203/0822 , C01B2203/1247 , C01B2203/1288 , C01B2203/142 , Y02P20/128 , Y02P20/133
摘要： The process and the installation for production of synthesis gas is a multi phased method of obtaining synthesis gas (to be referred from now on as syngas) in a continuous flow; the purpose of this gas is using it as an alternative fuel. This process consists of creating, by aid of an injector (3), a continuous flow of a mixture between water and a liquid classical fossil fuel. The liquid mixture is fed into a "rotating cavitation/vaporization device" (6) and is transformed into a continuous flow of a gaseous mixture. The gaseous mixture is further more, successively super-heated: at first in the cylindrical/toroidal (19) part of the double mantle/shell of a horizontal cylindrical furnace (25); the mixture is secondly super-heated in a reforming tube (12), placed inside the burning area (24) of the furnace. The cylindrical furnace (25) is coupled to the lid (17) of a "user boiler" (18) so as to facilitate the practical use of the hot gases resulting from the furnace burning area (24) of the cylindrical furnace (25). As a result, from the successive chemical processes of pyrolysis and of the non- catalytic reforming with steam at high temperatures of the hydrocarbon from the mixture, the syngas is produced. The syngas is then fed into a dualburner (11), replacing the consumption of classic fossil fuels. The classic fossil fuels are initially used to pre-heat the furnace, facilitating the temperatures necessary for the formation of syngas. The heat generated from the ignition and burning of syngas is used to maintain, in the cylindrical furnace (25), the temperatures necessary for the endothermic thermo chemical reactions that sustain the continuous flow of syngas. The heat resulting from the burning of syngas is also used to cogenerate thermal, electrical or/and mechanical energy.
摘要翻译：用于生产合成气的方法和安装是在连续流中获得合成气（现在称为合成气）的多阶段方法; 这种气体的目的是将其用作替代燃料。该过程包括通过喷射器（3）的帮助来创建水和液体经典化石燃料之间的混合物的连续流动。将液体混合物进料到“旋转空化/蒸发装置”（6）中并转化成气体混合物的连续流。气态混合物进一步被连续过热：首先在水平圆柱形炉（25）的双层/壳体的圆柱形/环形（19）部分中; 将混合物在重整管（12）中二次过热，放置在炉的燃烧区域（24）内。圆筒形炉（25）与“用户锅炉”（18）的盖（17）连接，以便于实际使用由圆筒炉（25）的炉膛区域（24）产生的热气体，。因此，从混合物的烃的高温下的热分解和非蒸汽重整与蒸汽的连续化学过程，产生合成气。然后将合成气送入双重燃烧器（11），代替经典化石燃料的消耗。经典的化石燃料最初用于预热炉，有助于形成合成气所需的温度。由合成气点燃和燃烧产生的热量用于在圆柱形炉（25）中保持维持合成气连续流动的吸热热化学反应所需的温度。合成气燃烧产生的热量也用于热能，电或/和机械能。

33. 发明申请

WO2014046644A1 C-O-H COMPOUND PROCESSING FOR HYDROGEN OR LIQUID FUEL PRODUCTION 审中-公开
标题翻译：用于氢或液体燃料生产的C-O-H化合物处理
公开(公告)号：WO2014046644A1
公开(公告)日：2014-03-27
申请号：PCT/US2012/055922
申请日：2012-09-18
申请人： PROTON POWER, INC. , WEAVER, Samuel C. , WEAVER, Samuel P. , WEAVER, Daniel C. , HENSLEY, Daniel L.
发明人： WEAVER, Samuel C. , WEAVER, Samuel P. , WEAVER, Daniel C. , HENSLEY, Daniel L.
IPC分类号： C01B3/24 , C01B3/50 , B01J7/00 , B01J4/00
CPC分类号： C01B3/24 , C01B2203/0272 , C01B2203/066 , C01B2203/1217 , C10B53/02 , C10J3/02 , C10J2300/0916 , C10J2300/0973 , C10L9/086 , Y02E50/14 , Y02P20/145
摘要： Methods and systems are disclosed for extracting hydrogen and/or liquid fuel from a compound comprising carbon, oxygen, and hydrogen ("C-O-H"). The compound may include cellulose, lignin, and/or hemicellulose, for example. The compound may include a waste stream that includes at least one C-O-H compound. Water may be combined with the C-O-H compound to produce a wet form of the C-O-H compound. The wet form of the C-O-H compound may be transferred into a reaction processing chamber. The wet form of the C-O-H compound may be heated within the reaction chamber such that elements of the C-O-H compound dissociate and react, with one reaction product comprising at least hydrogen gas and/or liquid fuel. Some embodiments may utilize non-oxidation reactions to produce the hydrogen and/or liquid fuel, such as hydrous pyrolysis reactions. The hydrogen gas and/or liquid fuel may be utilized to generate electrical power, heat, or power different types of engines.
摘要翻译：公开了从包含碳，氧和氢的化合物（“C-O-H”）中提取氢和/或液体燃料的方法和系统。该化合物可以包括例如纤维素，木质素和/或半纤维素。化合物可以包括包含至少一种C-O-H化合物的废物流。水可以与C-O-H化合物组合以产生湿形式的C-O-H化合物。 C-O-H化合物的湿形式可以转移到反应处理室中。可以在反应室内加热湿式C-O-H化合物，使得C-O-H化合物的元素解离和反应，一个反应产物至少包含氢气和/或液体燃料。一些实施例可以利用非氧化反应来产生氢气和/或液体燃料，例如含水热解反应。氢气和/或液体燃料可用于产生不同类型发动机的电力，热量或功率。

34. 发明申请

WO2011155962A1 VARIOUS METHODS AND APPARATUSES FOR AN ULTRA-HIGH HEAT FLUX CHEMICAL REACTOR 审中-公开
标题翻译：用于超高热通道化学反应器的各种方法和装置
公开(公告)号：WO2011155962A1
公开(公告)日：2011-12-15
申请号：PCT/US2010/059564
申请日：2010-12-08
申请人： SUNDROP FUELS, INC. , SIMMONS, Wayne, W. , PERKINS, Christopher , JOVANOVIC, Zoran , HILTON, Courtland, M. , POPP, Peter , SCHRAMM, Bryan, J. , TURNER, John, T.
发明人： SIMMONS, Wayne, W. , PERKINS, Christopher , JOVANOVIC, Zoran , HILTON, Courtland, M. , POPP, Peter , SCHRAMM, Bryan, J. , TURNER, John, T.
IPC分类号： B21D53/02
CPC分类号： C07C29/152 , C01B3/24 , C01B3/34 , C01B2203/0216 , C01B2203/0222 , C01B2203/0272 , C01B2203/0485 , C01B2203/0495 , C01B2203/061 , C01B2203/062 , C01B2203/0816 , C01B2203/0822 , C01B2203/0877 , C01B2203/0894 , C01B2203/1241 , C10G2300/1011 , C10G2300/807 , C10G2400/02 , C10J3/485 , C10J3/506 , C10J3/84 , C10J2200/152 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/0976 , C10J2300/0989 , C10J2300/1223 , C10J2300/1246 , C10J2300/1269 , C10J2300/1292 , C10J2300/1621 , C10J2300/1665 , C10J2300/1687 , C10J2300/1693 , C10J2300/1884 , C10J2300/1892 , F28D2021/0022 , Y02E50/18 , Y02P20/128 , Y02P20/129 , Y02P20/134 , Y02P20/145 , Y02P30/20 , C07C31/04
摘要： Various processes and apparatus are discussed for an ultra-high heat flux chemical reactor. A thermal receiver and the reactor tubes are aligned to 1 ) absorb and re-emit radiant energy, 2) highly reflect radiant energy, and 3) any combination of these, to maintain an operational temperature of the enclosed ultra-high heat flux chemical reactor. Particles of biomass are gasified in the presence of a steam carrier gas and methane in a simultaneous steam reformation and steam biomass gasification reaction to produce reaction products that include hydrogen and carbon monoxide gas using the ultra-high heat flux thermal energy radiated from the inner wall and then into the multiple reactor tubes. The multiple reactor tubes and cavity walls of the receiver transfer energy primarily by radiation absorption and re-radiation, rather than by convection or conduction, to the reactants in the chemical reaction to drive the endothermic chemical reaction flowing in the reactor tubes.
摘要翻译：讨论了超高热通量化学反应器的各种工艺和装置。热接收器和反应器管对准1）吸收和再发射辐射能，2）高度反射辐射能，3）任何组合，以保持封闭的超高热通量化学反应器的工作温度。生物质颗粒在蒸汽载体气体和甲烷的存在下在同时蒸汽重整和蒸汽生物质气化反应中气化，以产生包含氢气和一氧化碳气体的反应产物，使用从内壁辐射的超高热通量热能然后进入多个反应管。接收器的多个反应器管和空腔壁主要通过辐射吸收和再辐射而不是通过对流或传导将能量转移到化学反应中的反应物以驱动在反应器管中流动的吸热化学反应。

35. 发明申请

WO2011116689A1 一种通过热解将生物质制造合成气的工艺方法及系统审中-公开
公开(公告)号：WO2011116689A1
公开(公告)日：2011-09-29
申请号：PCT/CN2011/072061
申请日：2011-03-23
申请人：武汉凯迪工程技术研究总院有限公司 , 宋侃 , 姜满意 , 孙钦 , 张世荣 , 张海清 , 张金桥
发明人：宋侃 , 姜满意 , 孙钦 , 张世荣 , 张海清 , 张金桥
IPC分类号： C10J3/66 , C10B53/02 , C10B57/10 , C10B49/22 , C01B3/36
CPC分类号： C10B53/02 , C01B3/22 , C01B2203/0272 , C10B49/22 , C10C5/00 , C10G2300/1011 , C10K1/026 , C10K1/04 , C10K1/06 , Y02E50/14 , Y02P20/129 , Y02P20/145 , Y02P30/20

36. 发明申请

WO2011022761A1 METHOD AND APPARATUS FOR PLASMA DECOMPOSITION OF METHANE AND OTHER HYDROCARBONS 审中-公开
标题翻译：甲烷和其他烃类等离子体分解的方法与装置
公开(公告)号：WO2011022761A1
公开(公告)日：2011-03-03
申请号：PCT/AU2010/001076
申请日：2010-08-23
申请人： HOPE CELL TECHNOLOGIES PTY LTD , VANCINA, Robert
发明人： VANCINA, Robert
IPC分类号： C01B3/24 , B01J19/08 , C01B31/02
CPC分类号： B01J19/088 , B01J2219/0875 , B01J2219/0877 , C01B3/24 , C01B2203/0272 , C01B2203/0861 , C01B2203/1241 , H05H1/48 , H05H1/50
摘要： This invention relates to a process and an apparatus for generating hydrogen and synthetic carbon- free gas by plasma reforming -decomposing of Methane and other hydrocarbons for producing hydrogen and synthetic carbon-free gas through plasma discharge in hydrogen medium. The process involves applying an electrical potential between the electrodes while immersed in hydrogen medium. The plasma ionises the medium, thereby generating hydrogen and synthetic gas by decomposing of hydrogen medium. The process further involves controlling the process by relocating the generated plasma between two or more further electrodes.
摘要翻译：本发明涉及一种用于通过等离子体重整生成氢气和合成无碳气体的方法和装置 - 通过在氢介质中通过等离子体放电产生氢气和合成无碳气体的甲烷和其它烃。该方法包括在浸入氢介质中之间在电极之间施加电势。等离子体离子化介质，从而通过分解氢介质产生氢气和合成气。该方法进一步涉及通过将所产生的等离子体重新定位在两个或多个另外的电极之间来控制该过程。

37. 发明申请

WO2010063587A1 ANLAGE ZUR HERSTELLUNG VON SILIZIUM MIT VERBESSERTER RESSOURCENNUTZUNG 审中-公开
标题翻译：植物硅与提高资源使用生产
公开(公告)号：WO2010063587A1
公开(公告)日：2010-06-10
申请号：PCT/EP2009/065466
申请日：2009-11-19
申请人： EVONIK DEGUSSA GMBH , LANG, Jürgen, Erwin , RAULEDER, Hartwig , FRINGS, Bodo
发明人： LANG, Jürgen, Erwin , RAULEDER, Hartwig , FRINGS, Bodo
IPC分类号： B01J19/24 , C01B33/025
CPC分类号： B01J6/00 , B01J6/008 , B01J19/0013 , B01J2219/00006 , B01J2219/00117 , C01B3/22 , C01B33/025 , C01B2203/0272 , Y02P20/129 , Y02P20/13
摘要： Die vorliegende Erfindung betrifft eine Anlage zur Herstellung von Silizium, vorzugsweise hochreinem Silizium, insbesondere Solarsilizium, sowie ein Verfahren zur Herstellung von Silizium, vorzugsweise hochreinem Silizium insbesondere Solarsilizium, jeweils mit besonders effektiver Ressourcenausnutzung und verringerter Emission von Schadstoffen.
摘要翻译：本发明涉及一种用于生产硅的，优选高纯度硅，特别是太阳能级硅的植物，和用于生产硅的，优选高纯度硅，特别太阳能硅，每一个特别有效的资源利用和减少污染物的排放的方法。

38. 发明申请

WO2007044592A2 METHODS FOR TRANSFORMING ORGANIC COMPOUNDS USING A LIQUEFIED METAL ALLOY AND RELATED APPARATUS 审中-公开
标题翻译：用液态金属合金转化有机化合物的方法及相关装置
公开(公告)号：WO2007044592A2
公开(公告)日：2007-04-19
申请号：PCT/US2006039269
申请日：2006-10-10
申请人： FAIRSTOCK TECHNOLOGIES CORP , VYGONYAYLO ALEXANDR IVANOVICH
发明人： VYGONYAYLO ALEXANDR IVANOVICH
IPC分类号： C07C27/00
CPC分类号： C01B3/24 , B01J19/18 , B01J2219/00094 , B01J2219/00123 , B01J2219/00135 , B01J2219/00139 , C01B2203/0272 , C07C209/325 , C07C209/365 , C07C211/47
摘要： An organic compound can be transformed by an exposure to a heat flow that passed through a liquefied metal alloy. Provided are methods for transforming organic compounds and related apparatuses.
摘要翻译：有机化合物可通过暴露于通过液化金属合金的热流而转化。提供了用于转化有机化合物和相关装置的方法。

39. 发明申请

WO2006094137A1 METHOD FOR ON BOARD DECARBONIZATION OF HYDROCARBON FUELS IN A VEHICLE 审中-公开
标题翻译：一种用于车辆中烃类燃料脱盐的方法
公开(公告)号：WO2006094137A1
公开(公告)日：2006-09-08
申请号：PCT/US2006/007446
申请日：2006-02-28
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , AL-DAWOOD, Ali , AL-MUHAISH, Fahad
发明人： AL-DAWOOD, Ali , AL-MUHAISH, Fahad
IPC分类号： F02B43/08
CPC分类号： B01D53/005 , C01B3/24 , C01B3/26 , C01B3/36 , C01B2203/025 , C01B2203/0272 , C01B2203/0277 , C01B2203/0405 , C01B2203/049 , C01B2203/06 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0833 , C01B2203/085 , C01B2203/0861 , C01B2203/0883 , C01B2203/1217 , C01B2203/1241 , C01B2203/1247 , C01B2203/1276 , C01B2203/1288 , C01B2203/169 , Y02P20/128 , Y02T10/36
摘要： A method and apparatus for the reduction of carbon dioxide emissions by the on-board treatment of a portion or all of the hydrocarbon fuel used to power an internal combustion engine mounted in a conventional transportation vehicle, utilize known decarbonization technology to break the fuel's hydrogen-carbon bond. The compounds are then cooled and separated into (1) elemental carbon powder that is stored on-board for later recovery and industrial use, and (2) hydrogen, or a hydrogen-rich gas stream, that is burned as a fuel in the ICE and/or diverted to other on-board energy related applications.
摘要翻译：通过车载处理用于为安装在常规运输车辆中的内燃机供电的部分或全部碳氢燃料来减少二氧化碳排放的方法和装置利用已知的脱碳技术来破坏燃料的氢 - 碳键。然后将化合物冷却并分离成（1）元素碳粉末，其存储在板上用于随后的回收和工业应用，和（2）在ICE中作为燃料燃烧的氢或富氢气流和/或转用于其他车载能源相关应用。

40. 发明申请

WO2006031011A1 APPARATUS OF CATALYTIC GASIFICATION FOR REFINED BIOMASS FUEL AT LOW TEMPERATURE AND THE METHOD THEREOF 审中-公开
标题翻译：低温精炼生物质燃料的催化气化装置及其方法
公开(公告)号：WO2006031011A1
公开(公告)日：2006-03-23
申请号：PCT/KR2005/001808
申请日：2005-06-14
申请人： KOREA INSTITUTE OF ENERGY RESEARCH , KANG, Sung-Kyu , SHIN, Hyun-Dong
发明人： KANG, Sung-Kyu , SHIN, Hyun-Dong
IPC分类号： C10G1/00
CPC分类号： C10J3/56 , B01J23/02 , B01J23/34 , B01J23/745 , B01J23/75 , B01J23/78 , B01J37/04 , C01B2203/0272 , C10J3/482 , C10J3/54 , C10J3/84 , C10J2200/158 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0973 , C10J2300/0983 , C10J2300/0989 , C10J2300/1693 , C10J2300/1846 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , C10K1/024 , C10K1/026 , C10K1/046 , C10K1/08 , C10K1/18 , C10K1/20 , C10K3/02 , C10K3/023 , Y02P20/52
摘要： Disclosed is a gasification technique for converting biomass, which is difficult to treat, into clean gas fuel able to be burned in a cogeneration system. The gasification technique includes first stage fluidized-bed catalytic gasification, and second stage gasification of tar and catalytic reforming to convert nitrogen in tar, and HCN in a flammable gas into NH3, unlike conventional gasification techniques. In addition, since the temperature of a total gasification process is lower than a melting point of ash, powdery ash is generated and thus easily treated. Also, little heat is released due to the low process temperature, and therefore, a compact reactor may be designed to produce gas having a high caloric value. Further, the generated tar is recovered and reused in other processes, and the gas fuel contains a small amount of ammonia.
摘要翻译：公开了一种用于将难以处理的生物质转化成能够在热电联产系统中燃烧的清洁气体燃料的气化技术。气化技术包括第一阶段流化床催化气化，焦油和催化重整的第二阶段气化，将焦油中的氮和可燃气体中的HCN转化为NH 3，与常规气化技术不同。此外，由于总气化过程的温度低于灰分的熔点，因此产生粉状灰分，因此易于处理。此外，由于低的工艺温度，很少的热被释放，因此，可以设计紧凑的反应器来产生具有高热值的气体。此外，生成的焦油被回收并在其它方法中重复使用，并且气体燃料含有少量的氨。

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