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1. 发明授权

US08128896B2 Permselective membrane type reactor 有权
标题翻译：选择性膜式反应器
公开(公告)号：US08128896B2
公开(公告)日：2012-03-06
申请号：US12053840
申请日：2008-03-24
申请人： Toshiyuki Nakamura , Nobuhiko Mori , Osamu Sakai , Koichi Katsurayama , Takashi Ina , Koki Hamada
发明人： Toshiyuki Nakamura , Nobuhiko Mori , Osamu Sakai , Koichi Katsurayama , Takashi Ina , Koki Hamada
IPC分类号： B01J8/02 , B01J8/04
CPC分类号： B01D53/228 , B01D63/066 , B01D71/022 , B01D71/12 , B01D2255/10 , B01D2255/20738 , B01D2255/9022 , B01D2256/16 , B01D2325/10 , B01J19/2475 , B01J23/42 , B01J23/52 , B01J23/862 , B01J23/8993 , B01J37/0244 , B01J37/0248 , C01B3/16 , C01B2203/041 , Y02P20/52
摘要： There is disclosed a permselective membrane reactor which efficiently forms hydrogen by use of a water-gas shift reaction and which is excellent in an aspect of manufacturing cost. In a permselective membrane reactor, a permselective membrane is a Pd membrane or a Pd alloy membrane, and a catalyst layer includes a first catalyst layer on the side of the permselective membrane and a second catalyst layer disposed apart from the permselective membrane. The first catalyst layer has a noble metal-based catalyst, and the second catalyst layer has an iron-based catalyst.
摘要翻译：公开了通过使用水煤气变换反应有效地形成氢的选择性选择性膜反应器，在制造成本方面优异。在选择性选择性膜反应器中，选择性选择性膜是Pd膜或Pd合金膜，催化剂层包括在选择性渗透膜侧的第一催化剂层和与选择性渗透膜隔开的第二催化剂层。第一催化剂层具有贵金属类催化剂，第二催化剂层具有铁系催化剂。

2. 发明申请

US20120000358A1 STRUCTURE PROVIDED WITH ZEOLITE SEPARATION MEMBRANE, METHOD FOR PRODUCING SAME, METHOD FOR SEPARATING MIXED FLUIDS AND DEVICE FOR SEPARATING MIXED FLUIDS 有权
标题翻译：用沸石分离膜提供的结构，其生产方法，分离混合流体的方法和用于分离混合流体的装置
公开(公告)号：US20120000358A1
公开(公告)日：2012-01-05
申请号：US13231440
申请日：2011-09-13
申请人： Masaaki KAWAI , Toshihiro TOMITA , Nobuhiko MORI , Aya SATOH
发明人： Masaaki KAWAI , Toshihiro TOMITA , Nobuhiko MORI , Aya SATOH
IPC分类号： B01D71/04 , C01B39/00 , B01D19/00
CPC分类号： B01D53/228 , B01D63/066 , B01D67/0051 , B01D71/028 , B01D2323/42
摘要： There is provided a zeolite separation membrane-provided article having gaps or pores larger than pores inherent to zeolite crystals and controlled within an appropriate range and being capable of achieving both high permeability and high separability for components with small difference in adsorption properties or a component having a smaller molecular diameter than the diameter of the pores, a method for producing the same, a method for separating mixed fluids, and a device for separating mixed fluids. The zeolite separation membrane-provided article is provided with a zeolite membrane having an N2 gas permeation speed at room temperature of 1.0×10−6 mol·m−2·s−1·Pa−1 or more and a permeation speed ratio of 1,3,5-trimethylbenzene/N2 at room temperature of 0.17 or more and being free from dyeing caused by the impregnation with Rhodamine B.
摘要翻译：本发明提供一种沸石分离膜的制品，其具有比沸石晶体固有的孔隙大的孔隙，并且控制在适当的范围内，能够实现吸附性差的成分的高渗透性和高分离性，比孔的直径小的分子直径，其制造方法，分离混合流体的方法和用于分离混合流体的装置。在沸石分离膜的制品中，室温下的N 2气体透过速度为1.0×10 -6 mol·m-2·s -1·Pa -1以上且透过速度比为1的沸石膜，3,5-三甲基苯/ N 2在室温下为0.17以上，并且不被由罗丹明B浸渍引起的染色。

3. 发明申请

US20110204059A1 INTERNAL COMBUSTION ENGINE SYSTEM 审中-公开
标题翻译：内燃机系统
公开(公告)号：US20110204059A1
公开(公告)日：2011-08-25
申请号：US13023060
申请日：2011-02-08
申请人： Junichi KAMIO , Aya SATO , Nobuhiko MORI , Kiyoshi ARAKI
发明人： Junichi KAMIO , Aya SATO , Nobuhiko MORI , Kiyoshi ARAKI
IPC分类号： B65D25/04
CPC分类号： F02D41/0025 , F02D19/0665 , F02D19/0671 , F02D19/081 , F02D19/084 , Y02T10/36
摘要： Provided is an internal combustion engine system (1) capable of obtaining sufficient quantity of ethanol by separating a gasoline-ethanol composite fuel to gasoline and ethanol without being affected by components of gasoline. The internal combustion engine system (1) includes a composite fuel storing tank (2), a separation membrane (3) configured to separate a composite fuel to a gasoline component and an ethanol component, and a supplying unit (9) configured to supply the gasoline component and the ethanol component to an internal combustion engine respectively according to operation conditions. The separation membrane (3) is prepared to permeate aromatic hydrocarbons together with ethanol.
摘要翻译：提供一种内燃机系统（1），能够通过将汽油 - 乙醇复合燃料与汽油和乙醇分离而不受汽油成分的影响而获得足量的乙醇。内燃机系统（1）包括复合燃料储存罐（2），将复合燃料分离成汽油成分和乙醇成分的分离膜（3），以及供给部（9）汽油组分和乙醇组分分别根据操作条件分配给内燃机。制备分离膜（3）与乙醇一起渗透芳烃。

4. 发明授权

US08343348B2 Method for producing carbon film, carbon film and separator 有权
标题翻译：生产碳膜，碳膜和隔膜的方法
公开(公告)号：US08343348B2
公开(公告)日：2013-01-01
申请号：US13338692
申请日：2011-12-28
申请人： Aya Satoh , Nobuhiko Mori
发明人： Aya Satoh , Nobuhiko Mori
IPC分类号： B01D63/00 , B01D15/00 , B01D39/00 , B01D39/14 , B29C33/48 , B29C65/00
CPC分类号： C07B63/00 , B01D63/066 , B01D67/0067 , B01D71/021 , B01D2323/42 , C01B32/05 , C02F1/283 , C02F1/44 , C02F1/448 , C07C29/76 , C07C41/40 , C07C31/04 , C07C31/08 , C07C43/04
摘要： A method for producing a carbon membrane of the present invention is a production method where a carbon membrane obtained by subjecting a carbon-containing layer to thermal decomposition in an oxygen inert atmosphere while sending a gas mixture containing an oxidizing gas thereinto is thermally heated. The carbon membrane is subjected to a heating oxidation treatment with controlling the ratio of the flow rate of the gas mixture to the areas of the carbon membrane to 0.5 cm/min. or more to control (temperature ° C.)2×time (h)/10000, which is the relation between the temperature of the gas mixture and the flow time, to 9 to 32. This enables to obtain a carbon film which selectively separates alcohols having 2 or less carbon atoms from a liquid mixture of the alcohols having 2 or less carbon atoms and organic compounds having 5 to 9 carbon atoms.
摘要翻译：本发明的碳膜的制造方法是将氧气惰性气氛中的含碳层进行热分解同时送入含有氧化性气体的气体混合物而得到的碳膜热加热的制造方法。对碳膜进行加热氧化处理，控制气体混合物的流量与碳膜的面积的比例为0.5cm / min。以上，将气体混合物的温度与流动时间的关系的2×时间（h）/ 10000（温度℃）设定为9〜32。这样可以获得选择性分离的碳膜具有2个以下碳原子的醇的液体混合物和碳原子数5〜9的有机化合物的碳原子数2以下的醇。

5. 发明授权

US07560090B2 Process for producing hydrogen with permselective membrane reactor and permselective membrane reactor 有权
标题翻译：用选择性选择性膜反应器和选择性渗透膜反应器生产氢气的方法
公开(公告)号：US07560090B2
公开(公告)日：2009-07-14
申请号：US11956733
申请日：2007-12-14
申请人： Toshiyuki Nakamura , Nobuhiko Mori
发明人： Toshiyuki Nakamura , Nobuhiko Mori
IPC分类号： C01B3/22 , B01D53/22
CPC分类号： B01D53/22 , B01D2257/108 , B01J8/009 , B01J8/025 , B01J8/0257 , B01J2208/00415 , C01B3/323 , C01B3/505 , C01B2203/0227 , C01B2203/0233 , C01B2203/041 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/1052 , C01B2203/1064 , C01B2203/1229
摘要： A permselective membrane reactor is provided, including a reactor tube having a gas inlet at one end and a gas outlet at the other end thereof. A separator tube is disposed in the reactor tube and has a permselective membrane selectively permeable to hydrogen on a surface thereof and a discharge outlet for passing separated gas through the permselective membrane. The permselective membrane reactor also includes a layer comprising a reforming catalyst that promotes reforming of ethanol, so that β, defined by the following equation, is in a range of 0.05 to 20: β=a/b wherein a denotes the volume of the reforming catalyst layer [cm3], and b denotes the area of the permselective membrane [cm2].
摘要翻译：提供了一种选择性选择性膜反应器，包括一端具有气体入口的反应器管和在另一端的气体出口。分离管设置在反应器管中，并且具有在其表面上选择性地渗透氢气的选择性选择膜和用于使分离的气体通过选择性渗透膜的排出口。选择性选择性膜反应器还包括包含促进乙醇重整的重整催化剂的层，使得由下列等式定义的β在0.05至20的范围内：<？in-line-formula description =“In-line 公式“end =”lead“？> beta = a / b <？in-line-formula description =”In-line Formulas“end =”tail“？>其中a表示重整催化剂层的体积[cm3] b表示选择渗透膜的面积[cm2]。

6. 发明申请

US20090016941A1 Electrode Device For Plasma Discharge 审中-公开
标题翻译：等离子体放电用电极装置
公开(公告)号：US20090016941A1
公开(公告)日：2009-01-15
申请号：US12087487
申请日：2007-01-10
申请人： Michio Takahashi , Atsuo Kondo , Nobuhiko Mori
发明人： Michio Takahashi , Atsuo Kondo , Nobuhiko Mori
IPC分类号： B01J19/08
CPC分类号： C04B38/00 , B01D53/32 , B01D2256/16 , B01D2259/818 , C01B3/342 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0861 , C04B35/10 , C04B2111/00405 , C04B2111/00844 , H05H1/2406 , H05H2001/2418 , H05H2001/2437 , Y02P20/52 , C04B38/0074
摘要： It is disclosed a plasma discharging electrode device generating non-equilibrium plasma for treating a gas. The device has a substrate comprising an integrated sintered ceramic body; an electrode embedded in said substrate; and a catalyst supported by said substrate and accelerating the reaction of the gas. The substrate has a surface portion whose porosity is higher than that of a portion in the vicinity of the electrode in the substrate.
摘要翻译：公开了一种产生用于处理气体的非平衡等离子体的等离子体放电电极装置。该装置具有包括一体化的烧结陶瓷体的基板; 嵌入所述衬底中的电极; 以及由所述基材负载的催化剂并促进气体的反应。基板具有孔隙率高于基板中的电极附近的部分的表面部分。

7. 发明申请

US20080311014A1 PERMSELECTIVE MEMBRANE TYPE REACTOR 有权
标题翻译：选择性膜类反应器
公开(公告)号：US20080311014A1
公开(公告)日：2008-12-18
申请号：US12053840
申请日：2008-03-24
申请人： Toshiyuki Nakamura , Nobuhiko Mori , Osamu Sakai , Koichi Katsurayama , Takashi Ina , Koki Hamada
发明人： Toshiyuki Nakamura , Nobuhiko Mori , Osamu Sakai , Koichi Katsurayama , Takashi Ina , Koki Hamada
IPC分类号： B01J19/00
CPC分类号： B01D53/228 , B01D63/066 , B01D71/022 , B01D71/12 , B01D2255/10 , B01D2255/20738 , B01D2255/9022 , B01D2256/16 , B01D2325/10 , B01J19/2475 , B01J23/42 , B01J23/52 , B01J23/862 , B01J23/8993 , B01J37/0244 , B01J37/0248 , C01B3/16 , C01B2203/041 , Y02P20/52
摘要： There is disclosed a permselective membrane type reactor which efficiently forms hydrogen by use of a water-gas shift reaction and which is excellent in an aspect of manufacturing cost. In a permselective membrane type reactor 100, a permselective membrane 3 is a Pd membrane or a Pd alloy membrane, and a catalyst layer 4 includes a first catalyst layer 4a on the side of the permselective membrane 3 and a second catalyst layer 4b disposed apart from the permselective membrane 3. The first catalyst layer 4a has a noble metal-based catalyst, and the second catalyst layer 4b has an iron-based catalyst.
摘要翻译：公开了一种通过使用水煤气变换反应有效地形成氢并且在制造成本方面优异的透选膜型反应器。在选择性选择性膜型反应器100中，选择渗透膜3是Pd膜或Pd合金膜，催化剂层4包括在选择性渗透膜3侧的第一催化剂层4a和与第二催化剂层4b隔开的第二催化剂层4b 选择性选择膜3.第一催化剂层4a具有贵金属类催化剂，第二催化剂层4b具有铁基催化剂。

8. 发明申请

US20080050300A1 SELECTIVE PERMEATION MEMBRANE REACTOR AND METHOD OF MANUFACTURING HYDROGEN GAS 审中-公开
标题翻译：选择性渗透膜反应器和制造氢气的方法
公开(公告)号：US20080050300A1
公开(公告)日：2008-02-28
申请号：US11830243
申请日：2007-07-30
申请人： Toshiyuki NAKAMURA , Nobuhiko Mori
发明人： Toshiyuki NAKAMURA , Nobuhiko Mori
IPC分类号： C01B3/02 , C01B3/58
CPC分类号： C01B3/38 , B01J8/009 , B01J8/0214 , B01J8/0257 , B01J19/2475 , B01J2208/00539 , B01J2208/00548 , C01B3/501 , C01B3/586 , C01B2203/0233 , C01B2203/041 , C01B2203/0445 , C01B2203/047
摘要： There are disclosed a selective permeation membrane reactor which includes a selective permeation membrane having an excellent permeation performance and a separation performance with suppresses of methanation reaction of CO2 contained in hydrogen-containing gas to efficiently perform CO methanation reaction and manufacture highly pure hydrogen, and a method of manufacturing a hydrogen gas. The selective permeation membrane reactor includes a CO reducing unit for reducing carbon monoxide contained in concentrated hydrogen-containing gas; and the unit having a methanation catalyst layer which performs a methanation reaction to reduce carbon monoxide contained in the concentrated hydrogen-containing gas, and a reaction temperature control section for controlling temperature of the catalyst layer at 250° C. or more and 350° C. or less, thereby selectively treating carbon monoxide. As the methanation catalyst, Ru carried by a carrier made of alumina may be used.
摘要翻译：公开了一种选择性渗透膜反应器，其包括选择性渗透膜，其具有优异的渗透性能和分离性能，同时抑制含氢气体中含有的CO 2甲烷化反应以有效地进行CO甲烷化反应并制造高纯度氢气，以及制造氢气的方法。选择性渗透膜反应器包括用于还原含氢气体中所含的一氧化碳的CO还原单元; 具有进行甲烷化反应以还原含氢气体中所含的一氧化碳的甲烷化催化剂层的单元和用于控制催化剂层的温度在250℃以上且350℃以下的反应温度控制部以下，从而选择性地处理一氧化碳。作为甲烷化催化剂，可以使用由氧化铝构成的载体载持的Ru。

9. 发明授权

US4498189A Comparator suitable for a character recognition system 失效
标题翻译：比较器适合于字符识别系统
公开(公告)号：US4498189A
公开(公告)日：1985-02-05
申请号：US350037
申请日：1982-02-18
申请人： Nobuhiko Mori
发明人： Nobuhiko Mori
IPC分类号： G06K9/62 , G06F7/22 , G06K9/64
CPC分类号： G06F9/30021 , G06F7/22 , G06K9/6202 , G06K9/64
摘要： In a pattern matching method, the input pattern of a character is compared with each of a plurality of standard patterns to detect similarities and differences by counting the number of pattern elements which are or are not matched with each other. To do this, a high-speed comparator stores a plurality of comparing data in a memory, which is driven by a clock pulse train. The memory produces a plurality of sequence signals during each time interval when the clock pulses of a number responding to a plurality of comparing data are applied thereto. The first or last produced sequence signal is detected from among the plurality of sequence signals and is used to extract the maximum or minimum data.
摘要翻译：在图案匹配方法中，将字符的输入图案与多个标准图案中的每一个进行比较，以通过对彼此匹配或不匹配的图案元素的数量进行计数来检测相似和差异。为此，高速比较器将多个比较数据存储在由时钟脉冲串驱动的存储器中。当将响应于多个比较数据的数字的时钟脉冲施加到其上时，存储器在每个时间间隔期间产生多个序列信号。从多个序列信号中检测第一或最后产生的序列信号，并且用于提取最大或最小数据。

10. 发明授权

US08361197B2 Structure provided with zeolite separation membrane, method for producing same, method for separating mixed fluids and device for separating mixed fluids 有权
标题翻译：提供沸石分离膜的结构，其制造方法，分离混合流体的方法和用于分离混合流体的装置
公开(公告)号：US08361197B2
公开(公告)日：2013-01-29
申请号：US13231440
申请日：2011-09-13
申请人： Masaaki Kawai , Toshihiro Tomita , Nobuhiko Mori , Aya Satoh
发明人： Masaaki Kawai , Toshihiro Tomita , Nobuhiko Mori , Aya Satoh
IPC分类号： B01D53/22 , B01D71/02 , B01D19/00 , C01B39/04
CPC分类号： B01D53/228 , B01D63/066 , B01D67/0051 , B01D71/028 , B01D2323/42
摘要： There is provided a zeolite separation membrane-provided article having gaps or pores larger than pores inherent to zeolite crystals and controlled within an appropriate range and being capable of achieving both high permeability and high separability for components with small difference in adsorption properties or a component having a smaller molecular diameter than the diameter of the pores, a method for producing the same, a method for separating mixed fluids, and a device for separating mixed fluids. The zeolite separation membrane-provided article is provided with a zeolite membrane having an N2 gas permeation speed at room temperature of 1.0×10−6 mol·m−2·s−1·Pa−1 or more and a permeation speed ratio of 1,3,5-trimethylbenzene/N2 at room temperature of 0.17 or more and being free from dyeing caused by the impregnation with Rhodamine B.
摘要翻译：本发明提供一种沸石分离膜的制品，其具有比沸石晶体固有的孔隙大的孔隙，并且控制在适当的范围内，能够实现吸附性差的成分的高渗透性和高分离性，比孔的直径小的分子直径，其制造方法，分离混合流体的方法和用于分离混合流体的装置。在沸石分离膜的制品中，室温下的N 2气体透过速度为1.0×10 -6 mol·m-2·s -1·Pa -1以上且透过速度比为1的沸石膜，3,5-三甲基苯/ N 2在室温下为0.17以上，并且不被由罗丹明B浸渍引起的染色。

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