专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US09738569B2 Production of acrylic acid and ethanol from carbonaceous materials 有权
公开(公告)号：US09738569B2
公开(公告)日：2017-08-22
申请号：US14875086
申请日：2015-10-05
申请人： Stephane Marie-Rose , Esteban Chornet
发明人： Stephane Marie-Rose , Esteban Chornet
IPC分类号： C07C51/00 , C07C1/20 , C07C29/151 , C07C29/50 , C07C45/35 , C07C51/25 , C10K3/00 , C07C41/09
CPC分类号： C07C1/20 , C01B2203/0266 , C01B2203/0415 , C01B2203/0465 , C01B2203/0485 , C01B2203/049 , C01B2203/061 , C07C29/1518 , C07C29/50 , C07C41/09 , C07C45/35 , C07C51/252 , C10J2300/0916 , C10J2300/1665 , C10K3/006 , Y02E50/18 , Y02E50/32 , Y02P20/145 , Y02P30/42 , C07C31/04 , C07C47/22 , C07C57/04 , C07C31/08 , C07C11/06 , C07C43/043
摘要： A process for producing acrylic acid from carbonaceous materials such as biomass. The carbonaceous material, such as biomass, is gasified to produce synthesis gas. The synthesis gas then is subjected to a plurality of reactions to produce acrylic acid.

2. 发明授权

US09406957B2 Hydrogen extraction 有权
标题翻译：氢萃取
公开(公告)号：US09406957B2
公开(公告)日：2016-08-02
申请号：US12508032
申请日：2009-07-23
申请人： Gerald Peter Jackson , Jason Ryan Babcock , Joseph Matthew Zlotnicki
发明人： Gerald Peter Jackson , Jason Ryan Babcock , Joseph Matthew Zlotnicki
IPC分类号： B01D46/22 , C01B3/24 , C01B31/02 , F02B43/08 , F02M25/12 , H01M8/06 , B01D46/00 , H01M8/04
CPC分类号： H01M8/0612 , B01D46/0079 , B01D46/22 , C01B3/24 , C01B32/05 , C01B2203/0266 , C01B2203/04 , C01B2203/049 , C01B2203/0805 , C01B2203/085 , C01B2203/1235 , C01B2203/1247 , C01B2203/84 , F02B43/08 , F02M25/12 , H01M8/04022 , H01M8/0631 , Y02P20/128 , Y02T10/121 , Y02T10/166 , Y02T10/32
摘要： Representatively, a method of separating carbon from hydrocarbon molecules, the method including: heating hydrocarbon molecules beyond their boiling point; decomposing the heated hydrocarbon molecules to generate elemental or molecular carbon and hydrogen gas; separating at least some of the elemental or molecular carbon from the hydrogen gas; chemically reacting the hydrogen gas to produce heat; and applying some of the heat in carrying out said heating.
摘要翻译：代表性地是从烃分子中分离碳的方法，该方法包括：将烃分子加热超过其沸点; 分解加热的烃分子以产生元素或分子碳和氢气; 从氢气中分离出至少一些元素或分子碳; 使氢气化学反应产生热量; 并且在进行所述加热时施加一些热量。

3. 发明授权

US09212059B2 Method and apparatus for improving the efficiency of an SMR process for producing syngas while reducing the CO2 in a gaseous stream 有权
标题翻译：用于提高用于生产合成气的SMR方法的效率同时减少气流中的CO 2的方法和装置
公开(公告)号：US09212059B2
公开(公告)日：2015-12-15
申请号：US14224842
申请日：2014-03-25
申请人： Gyco, Inc.
发明人： Gary C. Young , Eric S. Wagner , John C. Wooley
IPC分类号： C01B3/48 , C07C29/151 , C12P7/06 , C01B3/34
CPC分类号： C01B3/48 , C01B3/34 , C01B2203/00 , C01B2203/0205 , C01B2203/0216 , C01B2203/0222 , C01B2203/0283 , C01B2203/0415 , C01B2203/0465 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/84 , C01B2203/86 , C07C29/1518 , C12P7/06 , Y02E50/17 , Y02P30/30 , C07C31/08
摘要： A system and method for increasing the production of Syngas from an SMR (Steam Methane Reforming) processing plant by providing CO2 as an additional feedstock, such as from an exhaust stream of a Corn-to-Ethanol plant, or from a power plant or industrial plant, like a cement plant. The CO2 steam and methane are introduced into the SMR reactor heated to about 870° C. and at about one atmosphere such that a reaction takes place that produces Syngas comprising CO, Hydrogen (H2) and carbon dioxide (CO2). The Syngas is then cleaned and provided to a Fischer-Tropsch synthesis reactor or other Bio-catalytic synthesis reactor to produce Ethanol or other high value liquid fuel.
摘要翻译：通过提供二氧化碳作为附加原料，例如从玉米对乙醇装置的废气流，或从发电厂或工业中提高合成气从SMR（蒸汽甲烷重整）处理厂的生产的系统和方法植物，如水泥厂。将CO 2蒸汽和甲烷引入加热至约870℃的SMR反应器中，并在约一个大气压下进行，产生产生包含CO，氢（H 2）和二氧化碳（CO 2）的合成气的反应。然后将合成气清洗并提供给费 - 托合成反应器或其他生物催化合成反应器以生产乙醇或其它高价值液体燃料。

4. 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。

5. 发明授权

US09150488B2 Production of acrylic acid and ethanol from carbonaceous materials 有权
标题翻译：从碳质材料生产丙烯酸和乙醇
公开(公告)号：US09150488B2
公开(公告)日：2015-10-06
申请号：US13894567
申请日：2013-05-15
申请人： Stephane Marie-Rose , Esteban Chornet
发明人： Stephane Marie-Rose , Esteban Chornet
IPC分类号： C07C51/493 , C07C29/151 , C07C29/50 , C07C45/35 , C07C51/25 , C01B3/22 , C07C29/00 , C07C1/20 , C10K3/00
CPC分类号： C07C51/493 , C01B3/22 , C01B2203/0266 , C01B2203/0485 , C01B2203/049 , C01B2203/061 , C07C1/20 , C07C29/00 , C07C29/1518 , C07C29/50 , C07C45/35 , C07C51/252 , C10J2300/0916 , C10J2300/1665 , C10K3/006 , Y02E50/18 , Y02E50/32 , Y02P20/145 , C07C31/04 , C07C47/22 , C07C57/04 , C07C31/08 , C07C11/06
摘要： A process for producing acrylic acid from carbonaceous materials such as biomass. The carbonaceous material, such as biomass, is gasified to produce synthesis gas. The synthesis gas then is subjected to a plurality of reactions to produce acrylic acid.
摘要翻译：由碳质材料如生物质制备丙烯酸的方法。碳质材料如生物质被气化以产生合成气。然后对合成气进行多次反应以制备丙烯酸。

6. 发明授权

US09074148B2 Hydrogen and carbon utilization in synthetic fuels production plants 有权
标题翻译：合成燃料生产厂的氢和碳利用
公开(公告)号：US09074148B2
公开(公告)日：2015-07-07
申请号：US13248547
申请日：2011-09-29
申请人： Sergio Mohedas , Mark Ibsen
发明人： Sergio Mohedas , Mark Ibsen
IPC分类号： C01B3/34 , C01B3/56 , B01J37/16 , C10G49/02 , C10J3/00 , B01J37/18 , C10G2/00 , C10G45/60 , C10G47/02 , C10K3/00
CPC分类号： C10J3/00 , B01J37/16 , B01J37/18 , C01B3/34 , C01B3/56 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0485 , C01B2203/049 , C01B2203/062 , C10G2/332 , C10G45/60 , C10G47/02 , C10G49/02 , C10G2300/1011 , C10G2300/703 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/1618 , C10J2300/1659 , C10J2300/1823 , C10K3/00 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A system including at least one hydrogen extraction unit comprising an inlet for a synthesis feedgas from a synthesis feedgas line and adapted to remove at least one hydrogen-rich gas and at least one hydrogen-lean gas from the synthesis feedgas to yield a refined synthesis gas; and at least one hydrocarbon synthesis reactor, at least one dedicated activation reactor, or both, wherein the at least one hydrocarbon synthesis reactor is fluidly connected with the at least one hydrogen extraction unit and configured to provide liquid hydrocarbons and a first byproduct gas from a synthesis reactor feedstream comprising at least a portion of the refined synthesis gas; and wherein the at least one dedicated activation reactor is fluidly connected with the at least one hydrogen extraction unit, the at least one hydrocarbon synthesis reactor, or both, and configured for activation of hydrocarbon synthesis catalyst via an activation gas.
摘要翻译：一种包括至少一个氢气提取单元的系统，其包括用于从合成进料气管线合成进料气的入口，并适于从合成进料气中除去至少一种富氢气体和至少一种贫贫气体，以产生精制合成气 ; 和至少一个烃合成反应器，至少一个专用活化反应器或两者，其中所述至少一个烃合成反应器与所述至少一个氢提取单元流体连接并且构造成提供液体烃和来自第一副产物气体的第一副产物气体合成反应器进料流，其包含至少一部分精制合成气; 并且其中所述至少一个专用活化反应器与所述至少一个氢提取单元，所述至少一个烃合成反应器或两者流体连接，并且被配置为经由活化气体活化烃合成催化剂。

7. 发明授权

US08888872B2 Gasifier cooling system 有权
标题翻译：气化器冷却系统
公开(公告)号：US08888872B2
公开(公告)日：2014-11-18
申请号：US12831189
申请日：2010-07-06
申请人： Wei Chen , Richard Anthony DePuy , Judeth Brannon Corry , Benjamin Campbell Steinhaus
发明人： Wei Chen , Richard Anthony DePuy , Judeth Brannon Corry , Benjamin Campbell Steinhaus
IPC分类号： B01J7/00 , C01B3/36 , C10J3/74 , C10J3/76 , C10J3/86 , C10K3/04
CPC分类号： C01B3/36 , C01B2203/0216 , C01B2203/0255 , C01B2203/0283 , C01B2203/0485 , C01B2203/049 , C01B2203/061 , C01B2203/068 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/169 , C01B2203/84 , C10J3/74 , C10J3/76 , C10J3/86 , C10J2300/0916 , C10J2300/0959 , C10J2300/1606 , C10J2300/1618 , C10J2300/1653 , C10J2300/1656 , C10J2300/1675 , C10J2300/1678 , C10J2300/1861 , C10J2300/1892 , C10K3/04 , Y02E20/16 , Y02E20/18
摘要： A system, including, a gasifier, including: a gasification region, an inner wall surrounding the gasification region, and a first fuel path extending along the inner wall, wherein the first fuel path is configured to flow a first fuel to cool the gasifier, and the gasifier is configured to inject the first fuel from the first fuel path into the gasification region.
摘要翻译：一种包括气化器的系统，包括：气化区域，围绕所述气化区域的内壁和沿着所述内壁延伸的第一燃料路径，其中所述第一燃料路径被配置为使第一燃料流动以冷却所述气化器，并且所述气化器构造成将所述第一燃料从所述第一燃料路径喷射到所述气化区域中。

8. 发明申请

US20140288196A1 Method and Apparatus for Improving the Efficiency of an SMR Process for Producing Syngas While Reducing the CO2 in a Gaseous Stream 有权
标题翻译：用于提高生产合成气的SMR工艺的效率的方法和装置，同时减少气流中的CO 2
公开(公告)号：US20140288196A1
公开(公告)日：2014-09-25
申请号：US14224842
申请日：2014-03-25
申请人： Gyco, Inc.
发明人： Gary C. Young , Eric S. Wagner , John C. Wooley
IPC分类号： C07C29/151 , C01B3/48
CPC分类号： C01B3/48 , C01B3/34 , C01B2203/00 , C01B2203/0205 , C01B2203/0216 , C01B2203/0222 , C01B2203/0283 , C01B2203/0415 , C01B2203/0465 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/84 , C01B2203/86 , C07C29/1518 , C12P7/06 , Y02E50/17 , Y02P30/30 , C07C31/08
摘要： A system and method for increasing the production of Syngas from an SMR (Steam Methane Reforming) processing plant by providing CO2 as an additional feedstock, such as from an exhaust stream of a Corn-to-Ethanol plant, or from a power plant or industrial plant, like a cement plant. The CO2 steam and methane are introduced into the SMR reactor heated to about 870° C. and at about one atmosphere such that a reaction takes place that produces Syngas comprising CO, Hydrogen (H2) and carbon dioxide (CO2). The Syngas is then cleaned and provided to a Fischer-Tropsch synthesis reactor or other Bio-catalytic synthesis reactor to produce Ethanol or other high value liquid fuel.
摘要翻译：通过提供二氧化碳作为附加原料，例如从玉米对乙醇装置的废气流，或从发电厂或工业中提高合成气从SMR（蒸汽甲烷重整）处理厂的生产的系统和方法植物，如水泥厂。将CO 2蒸汽和甲烷引入加热至约870℃的SMR反应器中并在约一个大气压下进行，从而产生产生包含CO，氢（H 2）和二氧化碳（CO 2）的合成气的反应。然后将合成气清洗并提供给费 - 托合成反应器或其他生物催化合成反应器以生产乙醇或其它高价值液体燃料。

9. 发明申请

US20140250785A1 IN-SITU GASIFICATION OF SOOT CONTAINED IN EXOTHERMICALLY GENERATED SYNGAS STREAM 审中-公开
标题翻译：在异常生成的SYNGAS STREAM中包含的SOT的原位气化
公开(公告)号：US20140250785A1
公开(公告)日：2014-09-11
申请号：US14286530
申请日：2014-05-23
申请人： William Robert Licht , Shankar Nataraj , Xiang-Dong Peng , John Michael Repasky
发明人： William Robert Licht , Shankar Nataraj , Xiang-Dong Peng , John Michael Repasky
IPC分类号： C10K1/02
CPC分类号： C10K1/02 , C01B3/36 , C01B2203/0233 , C01B2203/0255 , C01B2203/04 , C01B2203/049 , C01B2203/0838 , C01B2203/141 , C10J3/466 , C10J3/721 , C10J3/84 , C10J2200/06 , C10J2300/094 , C10J2300/0983 , C10J2300/1846 , C10K3/003
摘要： A system is set forth for the exothermic generation of soot depleted syngas comprising (i) reacting a hydrocarbon-containing fuel with an oxygen containing gas in a first reactor to produce the syngas and byproducts comprising CO2, H2O and soot; and (ii) introducing the syngas and byproducts into a second reactor containing a non-carbonaceous material that traps the soot for a sufficient time such that the majority of the byproduct soot is gasified via reaction with the byproduct CO2 and/or H2O to produce a syngas stream that is depleted in the soot. The system is particularly suitable for the practice of heat exchange reforming therein a portion of the heat is recovered from the soot depleted syngas stream and used as at least a portion of the heat to facilitate the additional production of syngas via the (endothermic) catalytic reforming of natural gas and steam.
摘要翻译：阐述了用于放出产生不含烟灰的合成气的系统，其包括（i）在第一反应器中使含烃燃料与含氧气体反应以产生合成气和包含CO 2，H 2 O和烟灰的副产物; 和（ii）将合成气和副产物引入到含有非碳质材料的第二反应器中，所述非碳质材料捕集烟灰足够的时间，使得大部分副产物烟灰通过与副产物CO 2和/或H 2 O反应产生气化在烟灰中耗尽的合成气流。该系统特别适用于热交换重整的实践，其中一部分热量从除去烟灰的合成气流中回收并用作至少一部分热量，以促进通过（吸热）催化重整来额外生产合成气的天然气和蒸汽。

10. 发明申请

US20140217327A1 PROCESS FOR PRODUCTION OF SYNTHESIS GAS 有权
标题翻译：生产合成气的方法
公开(公告)号：US20140217327A1
公开(公告)日：2014-08-07
申请号：US14130942
申请日：2012-07-05
申请人： Hans Jurgen Mass , Volker Goke , Otto Machhammer , Marcus Guzmann , Christian Schneider , Wolfgang Alois Hormuth , Andreas Bode , Dirk Klingler , Matthias Kern , Grigorios Kolios
发明人： Hans Jurgen Mass , Volker Goke , Otto Machhammer , Marcus Guzmann , Christian Schneider , Wolfgang Alois Hormuth , Andreas Bode , Dirk Klingler , Matthias Kern , Grigorios Kolios
IPC分类号： C01B3/34
CPC分类号： C01B3/344 , C01B32/40 , C01B2203/0222 , C01B2203/042 , C01B2203/0425 , C01B2203/049 , C01B2203/0822 , C01B2203/085 , C01B2203/0872 , C01B2203/1241 , Y02P20/128 , Y02P20/584
摘要： Process for the production of synthesis gas (3), in which methane and carbon dioxide (2) are introduced into a reaction space (R) and reacted in the presence of a solid (W) at elevated temperatures to give hydrogen and carbon monoxide. Methane and carbon dioxide are passed through a carbon-containing granular material (W) and reacted in a high-temperature zone (H).
摘要翻译：制备合成气（3）的方法，其中将甲烷和二氧化碳（2）引入反应空间（R）并在固体（W）存在下在升高的温度下反应，得到氢气和一氧化碳。甲烷和二氧化碳通过含碳颗粒材料（W）并在高温区（H）中反应。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式