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1. 发明申请

US20150337722A1 METHOD FOR PRODUCING A GASEOUS FUEL COMPRISING HYDROGEN FROM KINETIC AND/OR POTENTIAL ENERGY RECOVERED FROM A VEHICLE POWERED BY A FOUR STROKE DIESEL ENGINE FITTED WITH AN ENGINE BRAKING MECHANISM AND SYSTEM USEFUL TO IMPLEMENT SUCH METHOD 有权
标题翻译：生产包含氢的动力和/或潜在能量的气体燃料的方法，该动力学和/或潜在能量由配备发动机制动机构的四冲程柴油发动机所驱动的动力和用于实施该方法的系统
公开(公告)号：US20150337722A1
公开(公告)日：2015-11-26
申请号：US14443521
申请日：2013-11-15
申请人： WALDERSON MIAMI LLC
发明人： Carlos Manuel Bastos
IPC分类号： F02B43/00 , F02M21/02 , C01B3/30
CPC分类号： F02B43/00 , B01J8/067 , B01J2208/00221 , B01J2219/00006 , C01B3/30 , C01B3/384 , C01B2203/0233 , C01B2203/0833 , F02M21/0227 , F02M25/12 , Y02T10/121 , Y02T10/16 , Y02T10/32
摘要： A method for producing a hydrogen gaseous fuel from kinetic and/or potential energy recovered from a vehicle powered by a four stroke Diesel engine fitted with a Jacobs engine brake during a deceleration stage. Such a method comprises the following steps: a) providing a preheated steam flow; b) providing a gas flow from at least one chemical species used as preheated carbon and hydrogen source; c) mixing the gas flow from at least one chemical species used as carbon and hydrogen source from step a) with the steam flow from step b); d) reacting the mixture from step c) in the catalytic bed of a reforming reactor, heated by high temperature air from the compression stage of the Diesel engine acting as engine brake upon deceleration, producing an outlet synthesis gas flow which contains hydrogen; e) causing water to condense in the outlet synthesis gas flow which contains hydrogen, producing a water-free synthesis gas flow, and f) storing the synthesis gas flow obtained at step e) in a reservoir for its subsequent use during an acceleration stage of the vehicle. A system useful to implement the method for recovering kinetic and/or potential energy from a vehicle powered by a four stroke Diesel engine fitted with a Jacobs engine brake during a deceleration stage.
摘要翻译：一种从在由减速阶段装配有雅可比发动机制动器的四冲程柴油发动机驱动的车辆中回收的动能和/或势能产生氢气体燃料的方法。这种方法包括以下步骤：a）提供预热的蒸汽流; b）提供来自用作预热碳和氢源的至少一种化学物质的气流; c）将来自步骤a）的用作碳和氢源的至少一种化学物质的气流与来自步骤b）的蒸汽流混合; d）将来自步骤c）的混合物在重整反应器的催化床中反应，由减压时作为发动机制动的柴油发动机的压缩级的高温空气加热，产生含有氢气的出口合成气流; e）使水在包含氢气的出口合成气流中冷凝，产生无水合成气流，以及f）将步骤e）中获得的合成气流存储在储存器中，以便在加速阶段期间随后使用机动车。一种用于实现用于在由减速阶段装配有Jacobs发动机制动器的四冲程柴油发动机驱动的车辆中恢复动能和/或势能的方法的系统。

2. 发明授权

US09150800B2 Second stage gasifier in staged gasification and integrated process 有权
标题翻译：第二阶段气化炉和整合过程
公开(公告)号：US09150800B2
公开(公告)日：2015-10-06
申请号：US14102327
申请日：2013-12-10
申请人： Southern Company
发明人： Guohai Liu , Pannalal Vimalchand , WanWang Peng
IPC分类号： C10K3/02 , C10J3/48 , C10J3/72
CPC分类号： C10J3/482 , C01B3/30 , C01B2203/0277 , C01B2203/04 , C01B2203/049 , C10J3/721 , C10J2300/093 , C10J2300/0956 , C10J2300/0976 , C10J2300/0993 , C10J2300/1807 , C10K3/005 , Y02E20/18 , Y02P20/125
摘要： A second stage gasification unit in a staged gasification integrated process flow scheme and operating methods are disclosed to gasify a wide range of low reactivity fuels. The inclusion of second stage gasification unit operating at high temperatures closer to ash fusion temperatures in the bed provides sufficient flexibility in unit configurations, operating conditions and methods to achieve an overall carbon conversion of over 95% for low reactivity materials such as bituminous and anthracite coals, petroleum residues and coke. The second stage gasification unit includes a stationary fluidized bed gasifier operating with a sufficiently turbulent bed of predefined inert bed material with lean char carbon content. The second stage gasifier fluidized bed is operated at relatively high temperatures up to 1400° C. Steam and oxidant mixture can be injected to further increase the freeboard region operating temperature in the range of approximately from 50 to 100° C. above the bed temperature.
摘要翻译：公开了分级气化一体化工艺流程图和操作方法中的第二阶段气化单元以气化各种低反应性燃料。包含第二阶段气化单元在较高温度下工作，接近床层的灰熔融温度，为单体配置，操作条件和方法提供了足够的灵活性，以实现低反应性材料如沥青和无烟煤的总体转化率超过95％，石油残渣和焦炭。第二阶段气化单元包括固定的流化床气化器，其操作有具有贫碳含量的预定惰性床材料的充分湍流床。第二级气化器流化床在高达1400℃的较高温度下操作。可以注入蒸汽和氧化剂混合物，以进一步将干舷区域操作温度提高到高于床温度的约50至100℃的范围内。

3. 发明申请

US20140127121A1 METHOD FOR THE PARALLEL PRODUCTION OF HYDROGEN AND CARBON-CONTAINING PRODUCTS 有权
标题翻译：平行生产含氢和含碳产品的方法
公开(公告)号：US20140127121A1
公开(公告)日：2014-05-08
申请号：US14131124
申请日：2012-07-06
申请人： Hans-Juergen Maass , Volker Goeke , Otto Machhammer , Marcus Guzmann , Christian Schneider , Wolfgang Alois Hormuth , Andreas Bode , Drik Klingler , Matthias Kern , Grigorios Kolios
发明人： Hans-Juergen Maass , Volker Goeke , Otto Machhammer , Marcus Guzmann , Christian Schneider , Wolfgang Alois Hormuth , Andreas Bode , Drik Klingler , Matthias Kern , Grigorios Kolios
IPC分类号： C01B3/24 , C01B31/02
CPC分类号： C01B3/24 , C01B3/28 , C01B3/30 , C01B32/05 , C01B2203/0272 , C01B2203/04 , C01B2203/0425 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0866 , C01B2203/1235 , C01B2203/1258 , C10B57/005 , Y02P20/128
摘要： The invention relates to a process for parallel preparation of hydrogen and one or more carbonaceous products, in which hydrocarbons are introduced into a reaction space (R) and decomposed thermally to carbon and hydrogen in the presence of carbon-rich pellets (W). It is a feature of the invention that at least a portion of the thermal energy required for the hydrocarbon decomposition is introduced into the reaction space (R) by means of a gaseous heat carrier.
摘要翻译：本发明涉及氢和一种或多种碳质产物的并行制备方法，其中在富含碳的颗粒（W）的存在下，将烃引入反应空间（R）并热分解成碳和氢。本发明的一个特征是烃分解所需的热能的至少一部分通过气态热载体引入反应空间（R）。

4. 发明授权

US08002854B2 Thermocatalytic process for CO2-free production of hydrogen and carbon from hydrocarbons 有权
标题翻译：用于从碳氢化合物中无CO2生产氢和碳的热催化过程
公开(公告)号：US08002854B2
公开(公告)日：2011-08-23
申请号：US11648453
申请日：2006-12-29
申请人： Nazim Z. Muradov
发明人： Nazim Z. Muradov
IPC分类号： B01J7/00 , C01B3/36 , C01B6/24 , C01B3/02 , C01B3/24 , C01B3/26
CPC分类号： H01M8/0631 , B01J8/0055 , B01J8/24 , B01J8/26 , B01J8/28 , B01J8/388 , B01J19/2475 , B01J21/18 , B01J2208/00176 , B01J2208/00256 , B01J2208/00274 , B01J2219/00006 , C01B3/26 , C01B3/28 , C01B3/30 , C01B3/50 , C01B3/501 , C01B3/506 , C01B3/52 , C01B3/56 , C01B32/05 , C01B2203/0277 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/066 , C01B2203/0811 , C01B2203/0827 , C01B2203/10 , C01B2203/1041 , C01B2203/1241 , C01B2203/1247 , C01B2203/148 , H01M8/0612 , H01M8/0618 , H01M2008/1095 , Y02P20/584
摘要： A novel process and apparatus are disclosed for sustainable CO2-free production of hydrogen and carbon by thermocatalytic decomposition (dissociation, pyrolysis, cracking) of hydrocarbon fuels over carbon-based catalysts in the absence of air and/or water. The apparatus and thermocatalytic process improve the activity and stability of carbon catalysts during the thermocatalytic process and produce both high purity hydrogen (at least, 99.0 volume %) and carbon, from any hydrocarbon fuel, including sulfurous fuels. In a preferred embodiment, production of hydrogen and carbon is achieved by both internal and external activation of carbon catalysts. Internal activation of carbon catalyst is accomplished by recycling of hydrogen-depleted gas containing unsaturated and aromatic hydrocarbons back to the reactor. External activation of the catalyst can be achieved via surface gasification with hot combustion gases during catalyst heating. The process and apparatus can be conveniently integrated with any type of fuel cell to generate electricity.
摘要翻译：公开了一种新颖的方法和装置，用于在不存在空气和/或水的情况下通过碳基催化剂的碳氢化合物燃料的热分解（解离，热解，裂化）来可持续地不产生氢和碳。该装置和热催化方法提高了碳催化剂在热催化过程中的活性和稳定性，并且从任何烃燃料（包括亚硫燃料）产生高纯度氢（至少99.0体积％）和碳。在优选的实施方案中，氢和碳的生产通过碳催化剂的内部和外部活化来实现。碳催化剂的内部活化是通过将含有不饱和烃和芳族烃的贫氢气回流回反应器来完成的。催化剂的外部活化可以通过在催化剂加热期间用热燃烧气体进行表面气化来实现。该方法和设备可以方便地与任何类型的燃料电池集成以发电。

5. 发明授权

US07699975B2 Method and system of heating a fluid catalytic cracking unit for overall CO2 reduction 有权
标题翻译：加热流化催化裂化装置以减少总体CO2的方法和系统
公开(公告)号：US07699975B2
公开(公告)日：2010-04-20
申请号：US11962810
申请日：2007-12-21
申请人： Brian W. Hedrick
发明人： Brian W. Hedrick
IPC分类号： C10G51/04
CPC分类号： C10G11/182 , B01J29/90 , B01J38/30 , C01B3/26 , C01B3/30 , C01B2203/0277 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/0883 , C10G11/185 , C10J3/482 , C10J2300/16 , C10J2300/1618 , C10J2300/1671 , F01K13/00 , Y02E20/344 , Y02P20/128 , Y02P20/52 , Y02P20/584 , Y02P30/30 , Y02P30/446
摘要： In at least one embodiment of the present invention, a method of heating a FCC unit having a regenerator and a reactor for over CO2 reduction is provided. The method comprises compressing syngas to define compressed syngas. CO2 is separated from the compressed syngas to provide a first stream of gas comprising CO2. The first stream of gas is expanded with a second stream of gas comprising O2 to define a feed gas. The feed gas and an injected hydrocarbon feed are introduced to the regenerator having spent catalyst from the reactor. The regenerator is at gasification conditions to burn the injected hydrocarbon feed and coke from the spent catalyst producing the syngas and heat for operating the reactor at reaction temperatures.
摘要翻译：在本发明的至少一个实施方案中，提供了一种加热具有再生器的FCC单元和用于二氧化碳还原的反应器的方法。该方法包括压缩合成气以限定压缩的合成气。 CO 2与压缩的合成气分离以提供包含CO 2的第一气体流。第一气体气体用包含O 2的第二气体气流扩张以限定进料气体。将进料气体和注入的烃进料从反应器引入到具有废催化剂的再生器中。再生器在气化条件下燃烧注入的烃进料和来自废催化剂的焦炭，产生合成气，并在反应温度下操作反应器的热量。

6. 发明授权

US3966634A Gasification method 失效
标题翻译：气化法
公开(公告)号：US3966634A
公开(公告)日：1976-06-29
申请号：US508394
申请日：1974-09-23
申请人： Martin E. Sacks
发明人： Martin E. Sacks
IPC分类号： C01B3/22 , C01B3/30 , C10J3/54 , C07C1/02 , C10J3/12
CPC分类号： C10J3/54 , C01B3/22 , C01B3/30 , C10J3/482 , C10J3/66 , C10J3/74 , C10J3/78 , C10J3/84 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0993 , C10J2300/1606 , C10J2300/1662 , C10J2300/1807 , C10J2300/1884 , C10J2300/1892
摘要： Coal gasification process gives a waste water stream containing phenolic impurities. This stream is fed into contact with hot solid heat transfer particles to form superheated steam which is fed to the gasification zone.
摘要翻译：煤气化过程产生含有酚类杂质的废水流。将该料流与热固体传热颗粒接触以形成进料至气化区的过热蒸汽。

7. 发明授权

US3966633A Waste water processing 失效
标题翻译：废水处理
公开(公告)号：US3966633A
公开(公告)日：1976-06-29
申请号：US508395
申请日：1974-09-23
申请人： Louis D. Friedman
发明人： Louis D. Friedman
IPC分类号： C01B3/22 , C01B3/30 , C01B17/16 , C01C1/10 , C10J3/54 , C07C1/02 , C10J3/12
CPC分类号： C10J3/54 , C01B17/167 , C01B3/22 , C01B3/30 , C01C1/10 , C10J3/482 , C10J3/62 , C10K1/004 , C10K1/005 , C10K1/101 , C10K1/122 , C10K1/143 , C10K1/16 , C10K3/04 , C10G2300/1003 , C10J2300/093 , C10J2300/0943 , C10J2300/1215 , C10J2300/1615 , C10J2300/1662 , C10J2300/169 , C10J2300/1696
摘要： Waste water formed in the gasification of coal and containing ammonia, H.sub.2 S, and phenolic compounds is treated to remove H.sub.2 S and a substantial proportion of its ammonia, while leaving sufficient ammonia in the water to maintain a pH of at least 8 (such as up to about 10.5, preferably about 8.5 to 9), the ammoniacal water is then flashed into a stream of superheated steam being fed to gasification zone. At the high temperatures in the gasification zone the organic impurities are decomposed.
摘要翻译：在煤气化和含氨，H2S和酚类化合物中形成的废水经处理以除去H 2 S及其相当比例的氨，同时在水中留下足够的氨以保持pH至少为8（例如直至约10.5，优选约8.5至9），然后将氨水闪蒸成进料至气化区的过热蒸汽流。在气化区的高温下，有机杂质分解。

8. 发明授权

US3615298A Gasification of carbonaceous material 失效
标题翻译：碳化物质的气化
公开(公告)号：US3615298A
公开(公告)日：1971-10-26
申请号：US3615298D
申请日：1969-12-16
申请人： CONSOLIDATION COAL CO
发明人： BENSON HOMER E
IPC分类号： C01B3/06 , C01B3/10 , C01B3/30 , C01B3/44 , C01G49/08 , C07C1/00 , C10B57/18 , C10J1/213 , C10J3/00 , C01B1/08 , C07C9/04 , C10J3/46
CPC分类号： C10J1/213 , C01B3/061 , C01B3/063 , C01B3/10 , C01B3/105 , C01B3/30 , C01B3/44 , C01G49/08 , C07C1/00 , C10B57/18 , C10G11/18 , C10J3/00 , C10J3/482 , C10J3/725 , C10J3/78 , C10J2300/093 , C10J2300/0973 , C10J2300/1807 , Y02E60/36 , Y02P20/128 , C07C9/04
摘要： The reaction of steam with iron, or lower iron oxides, is conducted in the presence of carbonaceous solids by circulating the steam upwardly in countercurrent flow relationship with downwardly moving iron or lower iron oxides in a fluidized bed of the carbonaceous solids.

9. 发明授权

US3374052A System for solid particles-fluid contact operations 失效
标题翻译：固体颗粒 - 液体接触操作系统
公开(公告)号：US3374052A
公开(公告)日：1968-03-19
申请号：US52436065
申请日：1965-12-20
申请人： DEPT OF CHEMICAL ENGINEERING
发明人： LIANG-TSENG FAN , YUNG WEN CHIN
IPC分类号： B01J8/18 , C01B3/30 , C01B3/44 , C01B17/77 , C07C17/10 , C07C45/36 , C07C209/36
CPC分类号： C07C209/36 , B01J8/18 , C01B3/30 , C01B3/44 , C01B17/77 , C07C17/10 , C07C45/36 , Y10S423/16 , C07C19/01

10. 发明授权

US3197284A Fluidized catalytic hydrogen production 失效
标题翻译：流化催化氢气生产
公开(公告)号：US3197284A
公开(公告)日：1965-07-27
申请号：US12933061
申请日：1961-08-04
申请人： UNIVERSAL OIL PROD CO
发明人： JAMES HOEKSTRA
IPC分类号： C01B3/30 , C01B3/44
CPC分类号： C01B3/30 , C01B3/44

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