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    STRUCTURE PROVIDED WITH ZEOLITE SEPARATION MEMBRANE, METHOD FOR PRODUCING SAME, METHOD FOR SEPARATING MIXED FLUIDS AND DEVICE FOR SEPARATING MIXED FLUIDS
    2.
    发明申请
    STRUCTURE PROVIDED WITH ZEOLITE SEPARATION MEMBRANE, METHOD FOR PRODUCING SAME, METHOD FOR SEPARATING MIXED FLUIDS AND DEVICE FOR SEPARATING MIXED FLUIDS 有权
    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

    Applicant: Masaaki KAWAI ,  Toshihiro TOMITA ,  Nobuhiko MORI ,  Aya SATOH

    Inventor： Masaaki KAWAI ,  Toshihiro TOMITA ,  Nobuhiko MORI ,  Aya SATOH

    IPC: B01D71/04 ,  C01B39/00 ,  B01D19/00

    CPC classification number: B01D53/228 ,  B01D63/066 ,  B01D67/0051 ,  B01D71/028 ,  B01D2323/42

    Abstract: 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.

    Abstract translation: 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。

    INTERNAL COMBUSTION ENGINE SYSTEM
    3.
    发明申请
    INTERNAL COMBUSTION ENGINE SYSTEM 审中-公开
    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

    Applicant: Junichi KAMIO ,  Aya SATO ,  Nobuhiko MORI ,  Kiyoshi ARAKI

    Inventor： Junichi KAMIO ,  Aya SATO ,  Nobuhiko MORI ,  Kiyoshi ARAKI

    IPC: B65D25/04

    CPC classification number: F02D41/0025 ,  F02D19/0665 ,  F02D19/0671 ,  F02D19/081 ,  F02D19/084 ,  Y02T10/36

    Abstract: 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.

    Abstract translation: 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。

    Method for producing carbon film, carbon film and separator
    4.
    发明授权
    Method for producing carbon film, carbon film and separator 有权
    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

    Applicant: Aya Satoh ,  Nobuhiko Mori

    Inventor： Aya Satoh ,  Nobuhiko Mori

    IPC: B01D63/00 ,  B01D15/00 ,  B01D39/00 ,  B01D39/14 ,  B29C33/48 ,  B29C65/00

    CPC classification number: 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

    Abstract: 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.

    Abstract translation: 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。

    Process for producing hydrogen with permselective membrane reactor and permselective membrane reactor
    5.
    发明授权
    Process for producing hydrogen with permselective membrane reactor and permselective membrane reactor 有权
    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

    Applicant: Toshiyuki Nakamura ,  Nobuhiko Mori

    Inventor： Toshiyuki Nakamura ,  Nobuhiko Mori

    IPC: C01B3/22 ,  B01D53/22

    CPC classification number: 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

    Abstract: 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].

    Abstract translation: 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]。

    SELECTIVE PERMEATION MEMBRANE REACTOR AND METHOD OF MANUFACTURING HYDROGEN GAS
    8.
    发明申请
    SELECTIVE PERMEATION MEMBRANE REACTOR AND METHOD OF MANUFACTURING HYDROGEN GAS 审中-公开
    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

    Applicant: Toshiyuki NAKAMURA ,  Nobuhiko Mori

    Inventor： Toshiyuki NAKAMURA ,  Nobuhiko Mori

    IPC: C01B3/02 ,  C01B3/58

    CPC classification number: 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

    Abstract: 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.

    Abstract translation: 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。

    Comparator suitable for a character recognition system
    9.
    发明授权
    Comparator suitable for a character recognition system 失效
    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

    Applicant: Nobuhiko Mori

    Inventor： Nobuhiko Mori

    IPC: G06K9/62 ,  G06F7/22 ,  G06K9/64

    CPC classification number: G06F9/30021 ,  G06F7/22 ,  G06K9/6202 ,  G06K9/64

    Abstract: 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.

    Abstract translation: 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。

    PERMSELECTIVE MEMBRANE TYPE REACTOR AND METHOD FOR HYDROGEN PRODUCTION
    10.
    发明申请
    PERMSELECTIVE MEMBRANE TYPE REACTOR AND METHOD FOR HYDROGEN PRODUCTION 审中-公开
    选择性膜类型反应器和氢生产方法

    公开(公告)号：US20080226544A1

    公开(公告)日：2008-09-18

    申请号：US12045189

    申请日：2008-03-10

    Applicant: Toshiyuki Nakamura ,  Nobuhiko Mori ,  Manabu Yoshida

    Inventor： Toshiyuki Nakamura ,  Nobuhiko Mori ,  Manabu Yoshida

    IPC: C01B3/26 ,  B01J19/00

    CPC classification number: C01B3/384 ,  B01J8/0411 ,  B01J8/0492 ,  B01J8/0496 ,  B01J19/2475 ,  C01B3/501 ,  C01B13/0251 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/0475 ,  C01B2203/0495 ,  C01B2203/0811 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1241

    Abstract: A permselective membrane type reactor 100 comprises: a cylindrical reaction tube 1 having a gas inlet 11 at one end and a gas outlet 12 at the other end, a cylindrical, bottomed, separation tube 2 inserted into the reaction tube 1, which is made of a porous material and has a permselective membrane 3 at the surface, and a catalyst layer 4 provided between the reaction tube 1 and the separation tube 2, for promotion of chemical reaction. The reactor 100 further comprises, at a location apart from the permselective membrane 3, an oxygen-containing gas feeding section 20 which extends in the gas-flowing direction of the reaction tube 1 and feeds an oxygen-containing gas from multiple positions to the catalyst layer 4 in the gas-flowing direction.

    Abstract translation: 选择性选择性膜型反应器100包括：一端具有气体入口11和另一端的气体出口12的圆柱形反应管1，插入反应管1中的圆柱形有底分离管2，其由 多孔材料，并且在表面具有选择性选择膜3，以及设置在反应管1和分离管2之间的催化剂层4，用于促进化学反应。 反应器100还包括在与选择渗透膜3隔开的位置处的含氧气体供给部分20，其在反应管1的气体流动方向上延伸并将含氧气体从多个位置供给催化剂 层4在气体流动方向上。

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