公开(公告)号：EP3142966A1

公开(公告)日：2017-03-22

申请号：EP15792589.2

申请日：2015-05-12

申请人： Virdia, Inc.

发明人： JANSEN, Robert ,  LAPIDOT, Noa ,  LAWSON, James, Alan ,  ZVIELY, Michael ,  MATIS, Neta ,  MADSEN, Lee ,  HALLAC, Bassem ,  TRAVISANO, Philip

IPC分类号： C01B3/22

CPC分类号： C07C45/002 ,  C01B3/22 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/1076 ,  C01B2203/1211 ,  C01B2203/1217 ,  C07C5/03 ,  C07C29/172 ,  C07C29/175 ,  C07C2523/44 ,  C07C2523/72 ,  C07C2523/86 ,  C07D307/08 ,  Y02E60/324 ,  C07C49/10 ,  C07C9/15 ,  C07C31/20

摘要： The present disclosure relates to methods, processes, and systems for utilizing the dehydrogenation of 2-butanol for hydrogen consuming reactions of biomass or biomass-derived molecules.

摘要翻译： 本公开涉及利用二丁醇脱氢生物质或生物质衍生分子的氢消耗反应的方法，方法和系统。 本发明涉及利用2-丁醇脱氢以消耗氢，氢化或生物质或生物质衍生分子的氢化脱氧反应的方法，方法和系统。

公开(公告)号：EP2964569A4

公开(公告)日：2017-01-04

申请号：EP13855695

申请日：2013-11-11

申请人： PHILLIPS 66 CO ,  PAUL UCHENNA P ,  RANDOLPH BRUCE B ,  NELSON JON M ,  FJARE KRISTI A ,  SMITH DANIELLE K ,  CRAGUN MARK RUMEL ,  SADOK RICHARD D

发明人： RANDOLPH BRUCE B ,  FJARE KRISTI A ,  SMITH DANIELLE K ,  CRAGUN MARK RUMEL ,  SADOK RICHARD D

IPC分类号： C01B3/32

CPC分类号： C01B3/323 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1211 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229

公开(公告)号：EP3109932A1

公开(公告)日：2016-12-28

申请号：EP15752420.8

申请日：2015-02-13

申请人： Panasonic Corporation ,  Toto Ltd.

发明人： ONUMA, Shigenori ,  TANIGUCHI, Noboru ,  KANEKO, Yasushi ,  SUKAWA, Toru ,  SAKAI, Osamu ,  MIKAMI, Yuichi ,  SHIRAHAMA, Hiroshi ,  OTSUKA, Toshiharu

IPC分类号： H01M8/04 ,  H01M8/06 ,  H01M8/10 ,  H01M8/0662 ,  H01M8/04225

CPC分类号： H01M8/04373 ,  C01B3/382 ,  C01B2203/0244 ,  C01B2203/0495 ,  C01B2203/066 ,  C01B2203/067 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1252 ,  C01B2203/127 ,  C01B2203/1288 ,  C01B2203/148 ,  C01B2203/84 ,  H01M8/04097 ,  H01M8/04225 ,  H01M8/04619 ,  H01M8/04738 ,  H01M8/04776 ,  H01M8/04925 ,  H01M8/0618 ,  H01M8/0675

摘要： A fuel cell system (100) includes: a reformer (11) configured to generate a reformed gas using a raw material; a fuel cell (12) configured to generate electric power using the reformed gas; a raw material supply passage (13) through which the raw material supplied to the reformer (11) flows; a hydro-desulfurizer (10) configured to remove a sulfur component in the raw material supplied to the reformer (11); a recycle passage (14) through which a part of the reformed gas is supplied as a recycled gas to the raw material supply passage (13) provided upstream of the hydro-desulfurizer (10); a temperature detector (15) configured to detect a temperature of the hydro-desulfurizer 10; and a controller (30), wherein: when the temperature of the hydro-desulfurizer (10) reaches a predetermined temperature, the controller (30) increases a flow rate of the raw material from a predetermined flow rate by a flow rate corresponding to a flow rate of the recycled gas, and then, the controller (30) starts supplying the recycled gas to the recycle passage; and after the recycled gas reaches an upstream end of the recycle passage (14) through the raw material supply passage (13), the controller (30) returns the flow rate of the raw material to the predetermined flow rate.

摘要翻译： 燃料电池系统（100）包括：重整器（11），其被配置为使用原料生成重整气体; 燃料电池（12），其被配置为使用所述重整气体来产生电力; 供给至重整器（11）的原料流过的原料供给通路（13） 加氢脱硫装置（10），其用于除去向所述改性器（11）供给的原料中的硫成分; 再循环通道（14），部分重整气体作为再循环气体通过该再循环通道供应到设置在加氢脱硫器（10）上游的原料供应通道（13）; 温度检测器（15），其被配置为检测加氢脱硫器10的温度; 和控制器（30），其中：当所述加氢脱硫器（10）的温度达到预定温度时，所述控制器（30）将所述原料的流量从预定流量增加对应于 然后，控制器（30）开始将再循环气体供应到再循环通道; 并且在再循环气体通过原料供给通路（13）到达再循环通路（14）的上游端之后，控制器（30）使原料的流量返回到预定流量。

公开(公告)号：EP1583929B1

公开(公告)日：2016-09-21

申请号：EP03785439.5

申请日：2003-12-31

申请人： Dana Canada Corporation

发明人： RONG, Xiaoyang ,  CHEADLE, Brian, E.

IPC分类号： B01J8/06 ,  F28F9/22 ,  H01M8/0612 ,  H01M8/0668 ,  B01J8/04 ,  B01J8/00 ,  B01J8/02 ,  C01B3/38 ,  C01B3/48 ,  F28F9/02 ,  F28D7/16

CPC分类号： B01J8/0242 ,  B01J8/008 ,  B01J8/0278 ,  B01J8/0285 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0492 ,  B01J8/0496 ,  B01J8/067 ,  B01J2208/00194 ,  B01J2208/00221 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00849 ,  B01J2208/025 ,  C01B3/382 ,  C01B3/384 ,  C01B3/48 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0844 ,  C01B2203/0883 ,  C01B2203/1023 ,  C01B2203/1082 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1288 ,  C01B2203/142 ,  C01B2203/1604 ,  C01B2203/1685 ,  C01B2203/169 ,  C01B2203/82 ,  F28D7/1607 ,  F28D7/1669 ,  F28F9/0236 ,  F28F9/0241 ,  F28F9/22 ,  H01M8/0618 ,  H01M8/0668

公开(公告)号：EP3034155A1

公开(公告)日：2016-06-22

申请号：EP16151495.5

申请日：2008-06-10

申请人： NGK Insulators, Ltd.

发明人： NODA, Kenichi

IPC分类号： B01D53/22 ,  B01D71/02 ,  C01B3/50 ,  B01J19/24 ,  B01J8/02 ,  B01D69/02 ,  C22C5/04 ,  C01B3/38

CPC分类号： B01D71/022 ,  B01D53/228 ,  B01D69/02 ,  B01D2256/16 ,  B01D2323/08 ,  B01D2325/28 ,  B01J8/0257 ,  B01J19/2485 ,  B01J2208/00088 ,  B01J2219/00069 ,  C01B3/384 ,  C01B3/505 ,  C01B2203/0233 ,  C01B2203/04 ,  C01B2203/041 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/066 ,  C01B2203/0805 ,  C01B2203/1011 ,  C01B2203/1023 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1211 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1241 ,  C01B2203/1247 ,  C22C5/04 ,  Y02P20/52

摘要： A hydrogen separation membrane comprises a palladium alloy that includes at least palladium, silver as an added metal A, and copper as an added metal B. The content of silver in the palladium alloy is 10 to 40 parts by mass, based on 100 parts by mass of palladium, and the content of copper in the palladium alloy is 1 to 15 parts by mass, based on 100 parts by mass of palladium. The hydrogen separation membrane exhibits excellent hydrogen permeability and durability.

摘要翻译： 氢分离膜包括钯合金，其至少包括钯，作为添加的金属A的银和作为添加的金属B的铜。钯合金中的银的含量为10〜40质量份，基于100份 钯质量，钯合金中铜的含量相对于100质量份的钯为1〜15质量份。 氢分离膜表现出优异的氢渗透性和耐久性。

公开(公告)号：EP2964569A1

公开(公告)日：2016-01-13

申请号：EP13855695.6

申请日：2013-11-11

申请人： Phillips 66 Company ,  Paul, Uchenna P. ,  Randolph, Bruce B. ,  Nelson, Jon M. ,  Fjare, Kristi A. ,  Smith, Danielle K. ,  Cragun, Mark Rumel ,  Sadok, Richard, D.

发明人： RANDOLPH, Bruce B. ,  FJARE, Kristi A. ,  SMITH, Danielle K. ,  CRAGUN, Mark Rumel ,  SADOK, Richard D.

IPC分类号： C01B3/16

CPC分类号： C01B3/323 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1211 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229

摘要： A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200
∘ C to about 375
∘ C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.

摘要翻译： 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 分离步骤然后将气态产物分离成氢气和废气。

公开(公告)号：EP2897898A1

公开(公告)日：2015-07-29

申请号：EP12885015.3

申请日：2012-09-18

申请人： Proton Power, Inc.

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.

公开(公告)号：EP2890631A1

公开(公告)日：2015-07-08

申请号：EP13832056.9

申请日：2013-08-27

申请人： Element 1 Corp

发明人： EDLUND, David, J. ,  SCHLUTHER, Robert

IPC分类号： C01B3/50

CPC分类号： C01B3/32 ,  C01B3/501 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/044 ,  C01B2203/0445 ,  C01B2203/047 ,  C01B2203/0811 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/1633 ,  C01B2203/1647 ,  C01B2203/169

摘要： Hydrogen generation assemblies and their components are disclosed. In some embodiments, the assemblies may include a pump controller configured to select a flowrate from a plurality of flowrates based on detected pressure, and to operate the pump at the selected flowrate. In some embodiments, the assemblies may include a purge valve assembly configured to allow at least one pressurized gas to flow through a purge conduit from a pressurized gas assembly to a fuel processing assembly when power to the fuel processing assembly is interrupted. In some embodiments, the assemblies may include a damper controller configured to move a damper between fully open and closed positions based, at least in part, on detected temperature in a hydrogen-producing region. In some embodiments, the assemblies may include a reformer controller configured to operate a fuel processing assembly between run and standby modes based, at least in part, on detected pressure.

公开(公告)号：EP2823885A1

公开(公告)日：2015-01-14

申请号：EP13757174.1

申请日：2013-03-07

申请人： Oita University ,  Dowa Holdings Co., Ltd.

发明人： NAGAOKA, Katsutoshi ,  MIYAZAKI, Tatsuro ,  YANO, Takuya ,  IKARI, Kazumasa ,  UEYAMA, Toshihiko

IPC分类号： B01J23/76 ,  B01J23/63 ,  C01B3/40 ,  H01M8/06 ,  H01M8/12

CPC分类号： H01M8/0618 ,  B01J8/08 ,  B01J21/06 ,  B01J23/002 ,  B01J23/10 ,  B01J23/464 ,  B01J23/63 ,  B01J23/755 ,  B01J35/002 ,  B01J35/026 ,  B01J37/0072 ,  B01J37/0244 ,  B01J37/16 ,  B01J2208/00814 ,  B01J2523/00 ,  C01B3/326 ,  C01B3/40 ,  C01B2203/0227 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/066 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/142 ,  H01M2008/1293 ,  Y02E60/522 ,  Y02E60/525 ,  Y02P20/52 ,  B01J2523/3712 ,  B01J2523/41 ,  B01J2523/48

摘要： An object of the present invention is to provide a catalyst in which a reaction initiation temperature at which self-heating function is exhibited is low and which is capable of suppressing carbon accumulation even when a reaction is repeated. The catalyst of the present invention is a catalyst including a CeZr-based oxide, silicon, and a catalytically active metal, wherein the CeZr-based oxide satisfies Ce x Zr y O 2 (x + y = 1) and the silicon satisfies molar ratios of 0.02 ≤ Si/Zr and 0.01

摘要翻译： 本发明的目的是提供一种催化剂，其中显示自发热功能的反应起始温度低，并且即使当重复反应时也能够抑制碳积累。 本发明的催化剂是包含CeZr类氧化物，硅和催化活性金属的催化剂，其中CeZr类氧化物满足Ce x Zr y O 2（x + y = 1）且硅满足0.02≤Si/ Zr和0.01

公开(公告)号：EP2366447B1

公开(公告)日：2014-12-17

申请号：EP11170141.3

申请日：2008-03-27

申请人： Nippon Oil Corporation

发明人： Niitsuma, Takuya ,  Maekawa, Shunsuke ,  Kobori, Yoshihiro

IPC分类号： B01D53/047 ,  B01D53/22 ,  C01B3/56 ,  C01B3/38 ,  C01B31/20 ,  C01B3/50

CPC分类号： C01B3/56 ,  B01D53/047 ,  B01D53/226 ,  B01D53/229 ,  B01D2256/16 ,  B01D2257/504 ,  C01B3/382 ,  C01B3/384 ,  C01B3/501 ,  C01B32/50 ,  C01B2203/0205 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/066 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1076 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1258 ,  C01B2203/148 ,  Y02C10/08 ,  Y02C10/10 ,  Y02P20/152

摘要： When the production of hydrogen and the recovery of carbon dioxide are simultaneously performed by using as a raw material a carbon-containing fuel, the increase of the system cost is suppressed and the efficiency is improved. Disclosed is a method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, including: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel; a PSA step of separating, by using a pressure swing adsorption apparatus, the hydrogen-containing gas into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen; and a step of obtaining, by treating the PSA offgas with a hydrogen separation membrane and a carbon dioxide separation membrane, a second hydrogen-enriched gas that is a gas enriched in hydrogen and a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide. Also disclosed is an apparatus for embodying the method.