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1. 发明授权

US07884257B2 Method for producing ethylene and propylene 有权
标题翻译：生产乙烯和丙烯的方法
公开(公告)号：US07884257B2
公开(公告)日：2011-02-08
申请号：US12066991
申请日：2006-09-14
申请人： Yoshikazu Takamatsu , Kouji Nomura
发明人： Yoshikazu Takamatsu , Kouji Nomura
IPC分类号： C07C4/06
CPC分类号： B01J29/44 , B01J29/068 , B01J29/072 , B01J37/0009 , B01J2229/42 , C07C4/06 , C10G11/02 , C10G11/05 , C10G11/10 , C10G2300/1088 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , C07C11/04 , C07C11/06
摘要： The invention is to provide a catalyst for long-term, high-yield and stable production of ethylene and propylene in an efficient and simple method of catalytic conversion from a hydrocarbon material. The invention relates to a method for producing ethylene and propylene by contacting a hydrocarbon material that contains an olefin having from 4 to 12 carbon atoms in an amount of at least 20% by weight, with a zeolite-containing shaped catalyst satisfying the following requirements (1) to (4), in a reactor for catalytic conversion of that olefin: (1) the zeolite is an intermediate pore-size zeolite having a pore size of from 5 to 6.5 angstroms, (2) the zeolite does not substantially contain a proton, (3) the zeolite contains at least one metal selected from the group consisting of metals belonging to the Group IB of the Periodic Table, (4) the zeolite has a silica/alumina molar ratio (SiO2/Al2O3 molar ratio) of from 800 to 2,000.
摘要翻译：本发明提供一种用于从烃类材料进行催化转化的有效且简单的方法中长期，高产率和稳定地生产乙烯和丙烯的催化剂。本发明涉及一种生产乙烯和丙烯的方法，该方法是将含有至少20重量％的含有4-12个碳原子的烯烃的烃材料与满足以下要求的含沸石成型催化剂 1）至（4）中，在该烯烃的催化转化反应器中：（1）沸石是孔径为5至6.5埃的中间孔径沸石，（2）沸石基本上不含有质子，（3）沸石含有选自属于元素周期表第IB族的金属中的至少一种金属，（4）沸石的二氧化硅/氧化铝摩尔比（SiO 2 / Al 2 O 3摩尔比）为 800至2,000。

2. 发明授权

US07893311B2 Method for producing ethylene and propylene 有权
标题翻译：生产乙烯和丙烯的方法
公开(公告)号：US07893311B2
公开(公告)日：2011-02-22
申请号：US12067037
申请日：2006-09-14
申请人： Yoshikazu Takamatsu , Kouji Nomura
发明人： Yoshikazu Takamatsu , Kouji Nomura
IPC分类号： C07C4/06
CPC分类号： B01J29/44 , B01J29/068 , B01J29/072 , B01J35/002 , B01J37/0009 , B01J2229/42 , C07C4/06 , C10G11/05 , C10G11/10 , C10G2300/1088 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06
摘要： The invention is to provide a catalyst excellent in product producibility and selectivity, and in coking degradation resistance and regeneration degradation resistance, which is for production of ethylene and propylene through catalytic conversion from a hydrocarbon material. The invention relates to a method for producing ethylene and propylene through catalytic conversion from an olefin, by contacting a hydrocarbon material with a zeolite-containing shaped catalyst satisfying the following requirements (1) to (6), in a reactor: (1) the zeolite is an intermediate pore-size zeolite having a pore size of from 5 to 6.5 angstroms, (2) the zeolite does not substantially contain a proton, (3) the zeolite contains at least one metal selected from the group consisting of metals belonging to the Group IB of the Periodic Table, (4) the zeolite-containing shaped catalyst comprises silica as a binder, (5) the zeolite-containing shaped catalyst has a side-crush strength of at least 2.5 N/mm, (6) the zeolite-containing shaped catalyst has a sodium content of 500 ppm or less as an H-exchange type thereof.
摘要翻译：本发明提供一种产品生产性和选择性优异，耐焦化降解性和再生降解性优异的催化剂，其通过从烃类材料的催化转化而生产乙烯和丙烯。本发明涉及一种通过从烯烃催化转化生产乙烯和丙烯的方法，通过在反应器中使烃材料与满足以下要求（1）至（6）的含沸石成型催化剂接触：（1）沸石是孔径为5至6.5埃的中等孔径沸石，（2）沸石基本上不含质子，（3）沸石含有选自属于（4）含沸石的成型催化剂包括二氧化硅作为粘合剂，（5）含沸石的成形催化剂的侧面压碎强度为至少2.5N / mm，（6）含沸石的成形催化剂的H交换型的钠含量为500ppm以下。

3. 发明申请

US20100063340A1 METHOD FOR PRODUCING ETHYLENE AND PROPYLENE 有权
标题翻译：生产乙烯和丙烯的方法
公开(公告)号：US20100063340A1
公开(公告)日：2010-03-11
申请号：US12067037
申请日：2006-09-14
申请人： Yoshikazu Takamatsu , Kouji Nomura
发明人： Yoshikazu Takamatsu , Kouji Nomura
IPC分类号： C07C4/06
CPC分类号： B01J29/44 , B01J29/068 , B01J29/072 , B01J35/002 , B01J37/0009 , B01J2229/42 , C07C4/06 , C10G11/05 , C10G11/10 , C10G2300/1088 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06
摘要： The invention is to provide a catalyst excellent in product producibility and selectivity, and in coking degradation resistance and regeneration degradation resistance, which is for production of ethylene and propylene through catalytic conversion from a hydrocarbon material. The invention relates to a method for producing ethylene and propylene through catalytic conversion from an olefin, by contacting a hydrocarbon material with a zeolite-containing shaped catalyst satisfying the following requirements (1) to (6), in a reactor: (1) the zeolite is an intermediate pore-size zeolite having a pore size of from 5 to 6.5 angstroms, (2) the zeolite does not substantially contain a proton, (3) the zeolite contains at least one metal selected from the group consisting of metals belonging to the Group IB of the Periodic Table, (4) the zeolite-containing shaped catalyst comprises silica as a binder, (5) the zeolite-containing shaped catalyst has a side-crush strength of at least 2.5 N/mm, (6) the zeolite-containing shaped catalyst has a sodium content of 500 ppm or less as an H-exchange type thereof.
摘要翻译：本发明提供一种产品生产性和选择性优异，耐焦化降解性和再生降解性优异的催化剂，其通过从烃类材料的催化转化而生产乙烯和丙烯。本发明涉及一种通过从烯烃催化转化生产乙烯和丙烯的方法，通过在反应器中使烃材料与满足以下要求（1）至（6）的含沸石成型催化剂接触：（1）沸石是孔径为5至6.5埃的中等孔径沸石，（2）沸石基本上不含质子，（3）沸石含有选自属于（4）含沸石的成型催化剂包括二氧化硅作为粘合剂，（5）含沸石的成形催化剂的侧面压碎强度为至少2.5N / mm，（6）含沸石的成形催化剂的H交换型的钠含量为500ppm以下。

4. 发明申请

US20090182184A1 METHOD FOR PRODUCING ETHYLENE AND PROPYLENE 有权
标题翻译：生产乙烯和丙烯的方法
公开(公告)号：US20090182184A1
公开(公告)日：2009-07-16
申请号：US12066991
申请日：2006-09-14
申请人： Yoshikazu Takamatsu , Kouji Nomura
发明人： Yoshikazu Takamatsu , Kouji Nomura
IPC分类号： C07C4/02
CPC分类号： B01J29/44 , B01J29/068 , B01J29/072 , B01J37/0009 , B01J2229/42 , C07C4/06 , C10G11/02 , C10G11/05 , C10G11/10 , C10G2300/1088 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , C07C11/04 , C07C11/06
摘要： The invention is to provide a catalyst for long-term, high-yield and stable production of ethylene and propylene in an efficient and simple method of catalytic conversion from a hydrocarbon material. The invention relates to a method for producing ethylene and propylene by contacting a hydrocarbon material that contains an olefin having from 4 to 12 carbon atoms in an amount of at least 20% by weight, with a zeolite-containing shaped catalyst satisfying the following requirements (1) to (4), in a reactor for catalytic conversion of that olefin: (1) the zeolite is an intermediate pore-size zeolite having a pore size of from 5 to 6.5 angstroms, (2) the zeolite does not substantially contain a proton, (3) the zeolite contains at least one metal selected from the group consisting of metals belonging to the Group IB of the Periodic Table, (4) the zeolite has a silica/alumina molar ratio (SiO2/Al2O3 molar ratio) of from 800 to 2,000.
摘要翻译：本发明提供一种用于从烃类材料进行催化转化的有效且简单的方法中长期，高产率和稳定地生产乙烯和丙烯的催化剂。本发明涉及一种生产乙烯和丙烯的方法，该方法是将含有至少20重量％的含有4-12个碳原子的烯烃的烃材料与满足以下要求的含沸石成型催化剂 1）至（4）中，在该烯烃的催化转化反应器中：（1）沸石是孔径为5至6.5埃的中间孔径沸石，（2）沸石基本上不含有质子，（3）沸石含有选自属于元素周期表第IB族的金属中的至少一种金属，（4）沸石的二氧化硅/氧化铝摩尔比（SiO 2 / Al 2 O 3摩尔比）为 800至2,000。

5. 发明申请

US20140116662A1 SERPENTINE HEAT EXCHANGER 审中-公开
标题翻译： SERPENTINE热交换器
公开(公告)号：US20140116662A1
公开(公告)日：2014-05-01
申请号：US14124345
申请日：2012-05-21
申请人： Yoshikazu Takamatsu , Masayuki Nakamura
发明人： Yoshikazu Takamatsu , Masayuki Nakamura
IPC分类号： F28D1/047 , F28F1/10
CPC分类号： F28D1/0478 , F28D1/0308 , F28D1/0358 , F28F1/10 , F28F1/126 , F28F1/426 , F28F3/044 , F28F2225/04 , F28F2275/122
摘要： A serpentine heat exchanger includes a tube formed by bonding two press-molded tube sheets and folded back in a serpentine shape, and a corrugated fin arranged in a space enclosed by the tube that is folded-back. An inside of a folded-back portion of the tube includes a plurality of protrusions at a distance from one another, the protrusions protruding from one tube sheet and contacting the other tube sheet.
摘要翻译：蛇形热交换器包括通过粘合两个压模管板并以蛇形形状折回而形成的管，以及布置在被折叠的管包围的空间中的波纹状翅片。管的折回部分的内部包括彼此间隔一定距离的多个突起，突出部从一个管板突出并与另一个管板接触。

6. 发明授权

US08703311B2 Vehicle battery cooling device 有权
标题翻译：车载电池冷却装置
公开(公告)号：US08703311B2
公开(公告)日：2014-04-22
申请号：US12864133
申请日：2009-02-24
申请人： Masaru Sawaguchi , Kenichi Koui , Kazuhiko Matsumoto , Yoshikazu Takamatsu
发明人： Masaru Sawaguchi , Kenichi Koui , Kazuhiko Matsumoto , Yoshikazu Takamatsu
IPC分类号： B60K11/00
CPC分类号： H01M10/48 , B60K1/04 , B60K11/08 , B60K2001/005 , B60L1/003 , B60L1/02 , B60L3/003 , B60L3/0046 , B60L11/14 , B60L11/1868 , B60L11/1874 , B60L11/1875 , B60L2210/10 , B60L2210/40 , B60L2240/34 , B60L2240/36 , B60L2240/545 , B60L2240/547 , B60W2510/246 , H01M10/613 , H01M10/625 , H01M10/63 , H01M10/637 , H01M10/6556 , H01M10/6563 , H01M10/6568 , H01M10/663 , H01M10/667 , H01M16/00 , Y02T10/70 , Y02T10/7005 , Y02T10/7066 , Y02T10/7077 , Y02T10/7216 , Y02T10/7241
摘要： [Task] It is an object of the present invention to provide a vehicle battery cooling device even if a situation that cannot be compensated by ordinary cooling means occurs, the efficient cooling is performed and a battery temperature can be stabilized.[Means for Solving] A cooling system of a heat exchanger 18 and a cooling system of a sub radiator 12 are provided to perform the cooling of high-power battery 6. A battery controller 31 which processes the information such as a temperature sensor 33 and so forth switches the device to perform the cooling of high-power battery 6 from the cooling system of heat exchanger 18 to the cooling system of sub radiator 12.
摘要翻译： [任务]本发明的目的是提供一种汽车电池冷却装置，即使发生由普通冷却装置不能补偿的情况，执行有效的冷却并且可以稳定电池温度。 [解决手段]设置热交换器18的冷却系统和副散热器12的冷却系统，以执行大功率电池6的冷却。电池控制器31处理诸如温度传感器33和从而切换设备以执行从热交换器18的冷却系统到副散热器12的冷却系统的大功率电池6的冷却。

7. 发明授权

US08450551B2 Method for producing propylene 有权
标题翻译：生产丙烯的方法
公开(公告)号：US08450551B2
公开(公告)日：2013-05-28
申请号：US13254373
申请日：2010-03-01
申请人： Yoshikazu Takamatsu , Ryusuke Miyazaki
发明人： Yoshikazu Takamatsu , Ryusuke Miyazaki
IPC分类号： C07C6/00
CPC分类号： B01J29/90 , B01J29/40 , B01J29/42 , B01J29/44 , B01J37/0009 , B01J37/0045 , B01J38/14 , B01J2229/42 , C07C6/04 , C07C2529/70 , Y02P20/52 , Y02P20/584 , C07C11/06
摘要： The present invention provides in a method for producing propylene from a hydrocarbon raw material containing ethylene in an amount exceeding 50% by mass under the co-existence of water, a method for producing propylene stably over a long term from ethylene in a high yield and with the reaction/regeneration repeated. A method for producing propylene includes a step for catalytically converting a hydrocarbon raw material containing ethylene in an amount exceeding 50% by mass with a zeolite-containing catalyst while supplying water, wherein a zeolite contained in the zeolite-containing catalyst satisfies (1) to (3) shown below; (1) the zeolite is an MFI zeolite, (2) a zeolite crystallization index obtained from an X-ray diffraction spectrum is 3.3 or more, and (3) a molar ratio of silica/alumina (SiO2/Al2O3) is 20 to 300.
摘要翻译：本发明提供一种在水共存下含有乙烯量超过50质量％的烃类原料的丙烯的制造方法，从高产率从乙烯长期稳定生产丙烯的方法，以及反应/再生重复。丙烯的制造方法包括使含有沸石的催化剂同时供给水催化转化含有乙烯量超过50质量％的烃原料的工序，其中含有沸石的催化剂中所含的沸石满足（1）〜（3）如下所示; （1）沸石是MFI沸石，（2）从X射线衍射光谱获得的沸石结晶指数为3.3以上，（3）二氧化硅/氧化铝（SiO 2 / Al 2 O 3）的摩尔比为20〜300 。

8. 发明授权

US07000644B2 Flexible hose 失效
标题翻译：软管
公开(公告)号：US07000644B2
公开(公告)日：2006-02-21
申请号：US10743490
申请日：2003-12-23
申请人： Nobuo Ichimura , Hiromi Takasaki , Yoshikazu Takamatsu
发明人： Nobuo Ichimura , Hiromi Takasaki , Yoshikazu Takamatsu
IPC分类号： F16L11/00
CPC分类号： G06T3/4015 , B60H1/00571 , F16L33/2073 , F16L39/005 , F16L39/02
摘要： A flexible hose for use as a refrigerant passageway in a vehicular refrigerating cycle has an inner hose and an outer hose. The outer hose covers the inner hose with a space formed in a given distance. The outer hose and the inner hose are formed of resin having flexibility.
摘要翻译：用作车辆制冷循环中的制冷剂通道的柔性软管具有内软管和外软管。外软管覆盖内部软管，空间形成一定距离。外软管和内软管由具有柔性的树脂形成。

9. 发明申请

US20050200121A1 Double pipe forked part structure and method of making the same 失效
标题翻译：双管叉结构及其制作方法
公开(公告)号：US20050200121A1
公开(公告)日：2005-09-15
申请号：US11075044
申请日：2005-03-09
申请人： Nobuo Ichimura , Yoshikazu Takamatsu , Susumu Sato
发明人： Nobuo Ichimura , Yoshikazu Takamatsu , Susumu Sato
IPC分类号： B21D19/08 , B21D41/02 , F16L9/18 , F16L9/19 , F16L13/14 , F16L39/00 , F16L41/02
CPC分类号： B21D41/021 , F16L9/19 , F16L41/023 , Y10T29/49361
摘要： A forked part structure of a double pipe has an outer pipe, an inner pipe, a branch pipe and an open end portion of the outer pipe. The open end portion of the outer pipe has a substantially tubular inner pipe supporting portion to which the inner pipe is brazed, and a substantially tubular branch pipe supporting portion to which the branch pipe is brazed. The inner pipe supporting portion is located inward of a main portion of the outer pipe along an extending direction of the main portion of the outer pipe.
摘要翻译：双管的叉形部分结构具有外管，内管，支管和外管的开口端部。外管的开口端部具有大致管状的内管支撑部，内管被钎焊到该内管支撑部，以及分支管钎焊到其上的大致管状的支管支撑部。内管支撑部沿着外管的主要部分的延伸方向位于外管主体的内侧。

10. 发明授权

US08034987B2 Process for producing propylene and aromatic hydrocarbons, and producing apparatus therefor 有权
标题翻译：制备丙烯和芳烃的方法及其制备装置
公开(公告)号：US08034987B2
公开(公告)日：2011-10-11
申请号：US12086308
申请日：2007-01-12
申请人： Mitsuhiro Sekiguchi , Yoshikazu Takamatsu
发明人： Mitsuhiro Sekiguchi , Yoshikazu Takamatsu
IPC分类号： C07C2/52 , C07C4/02
CPC分类号： C10G63/04 , B01J29/44 , B01J2229/16 , B01J2229/186 , B01J2229/36 , C07C2/84 , C07C4/06 , C07C2529/40 , C07C2529/44 , C10G11/05 , C10G35/065 , C10G2300/1088 , C10G2300/4018 , C10G2300/4081 , C10G2400/20 , C10G2400/30 , Y02P20/52 , Y02P20/584 , C07C15/00 , C07C11/06
摘要： It is an object of the present invention to provide an improved process whereby the yield structure of the components can be varied by a simple method, and the products can be produced stably and efficiently in a process for producing propylene and aromatic hydrocarbons from a hydrocarbon feedstock containing C4-12 olefins using a medium pore diameter zeolite-containing catalyst. A process for producing is disclosed which comprises a propylene production step wherein a specific zeolite catalyst is used to remove a C4+ hydrocarbon component from a reaction mixture, and part of the hydrocarbon component is recycled as necessary without modification, and an aromatic hydrocarbon production step wherein all or a part of the C4+ hydrocarbon component is used as the raw material.
摘要翻译：本发明的目的是提供一种通过简单的方法可以改变组分的产率结构的改进方法，并且可以在从烃原料生产丙烯和芳族烃的方法中稳定和有效地制备产物含有中等孔径的含沸石催化剂的C4-12烯烃。公开了一种制备方法，其包括丙烯制备步骤，其中使用特定的沸石催化剂从反应混合物中除去C 4+烃组分，并且部分烃组分根据需要进行再循环，无需改性，以及芳烃生产步骤，其中全部或部分C4 +烃组分用作原料。

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