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

US5154902A Exhaust gas purifying catalyst and exhaust gas purifying process 失效
标题翻译：废气净化催化剂和废气净化工艺
公开(公告)号：US5154902A
公开(公告)日：1992-10-13
申请号：US680794
申请日：1991-04-03
申请人： Tomoyuki Inui , Hideaki Muraki , Shiroh Kondoh , Akio Isogai , Shinichi Matsumoto
发明人： Tomoyuki Inui , Hideaki Muraki , Shiroh Kondoh , Akio Isogai , Shinichi Matsumoto
IPC分类号： B01D53/94 , B01J23/78 , B01J29/035 , B01J29/04 , B01J29/072
CPC分类号： B01J29/072 , B01D53/9418 , B01J23/78 , B01D2251/208 , B01D2255/1023 , B01D2255/20761 , B01D2255/30
摘要： An exhaust gas purifying catalyst of this invention is a catalyst for mainly removing nitrogen oxides contained in exhaust gases, comprising: crystalline copper silicate expressed by the following composition formula;M.sub.n+m (Cu.sub.n Al.sub.m Si.sub.96-n-m O.sub.192).16H.sub.2 O, where M denotes one of sodium (Na) and potassium (K), and n+m
摘要翻译：本发明的废气净化催化剂是用于主要除去废气中所含的氮氧化物的催化剂，包括：由以下组成式表示的结晶硅酸铜; Mn + m（CunAlmSi96-n-mO192）.16H2O，其中M表示钠（Na）和钾（K）之一，n + m <27。本发明的废气净化方法采用上述结晶硅酸铜催化剂。废气净化催化剂和使用该废气净化催化剂的废气净化方法通过促进废气中所含的烃（HC）和氮氧化物（NOx）之间的反应比烃（HC）之间的反应更优先地净化氮氧化物（NOx））和氧（O 2），从而以高效率纯化氮氧化物（NO x）和烃（HC）。

2. 发明授权

US07700005B2 Oil-based thermo-neutral reforming with a multi-component catalyst 有权
标题翻译：用多组分催化剂进行油基热中性重整
公开(公告)号：US07700005B2
公开(公告)日：2010-04-20
申请号：US11645970
申请日：2006-12-26
申请人： Tomoyuki Inui , Bashir Osama Dabbousi , Shakeel Ahmed , Fahad Ibrahim Al-Muhaish , Mohammed Abdul Bari Siddiqui
发明人： Tomoyuki Inui , Bashir Osama Dabbousi , Shakeel Ahmed , Fahad Ibrahim Al-Muhaish , Mohammed Abdul Bari Siddiqui
IPC分类号： C01B3/26 , H01M8/04 , B01J23/10 , B01J21/08
CPC分类号： B01J23/8986 , B01J21/04 , B01J23/002 , B01J23/894 , B01J2523/00 , C01B3/382 , C01B2203/0238 , C01B2203/0244 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/06 , C01B2203/066 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1094 , C01B2203/1247 , C01B2203/1252 , Y02P20/52 , B01J2523/3706 , B01J2523/3712 , B01J2523/48 , B01J2523/74 , B01J2523/822 , B01J2523/828 , B01J2523/847
摘要： A method is provided for the thermo-neutral reforming of liquid hydrocarbon fuels which employs a Ni, Ce2O3, La2O3, Pt−ZrO2, Rh and Re catalyst having dual functionalities to achieve both combustion and steam reforming.
摘要翻译：提供了一种采用具有双重功能的Ni，Ce2O3，La2O3，Pt-ZrO2，Rh和Re催化剂的液体烃燃料的热中性重整方法，以实现燃烧和蒸汽重整。

3. 发明授权

US08329973B2 Multiple zeolite catalyst 有权
标题翻译：多重沸石催化剂
公开(公告)号：US08329973B2
公开(公告)日：2012-12-11
申请号：US13353085
申请日：2012-01-18
申请人： Tomoyuki Inui , Masayuki Inui, legal representative , Mohammad A. Ali , Muhammad A. Al-Saleh , Syed A. Ali , Khalid Al-Nawad , Tsutomo Okamoto , Katsuhiko Ishikawa , Minoru Hatayama
发明人： Tomoyuki Inui , Mohammad A. Ali , Muhammad A. Al-Saleh , Syed A. Ali , Khalid Al-Nawad , Tsutomo Okamoto , Katsuhiko Ishikawa , Minoru Hatayama
IPC分类号： C07C6/12
CPC分类号： B01J29/80 , B01J29/005 , B01J29/061 , B01J29/064 , B01J29/076 , B01J29/18 , B01J29/26 , B01J29/40 , B01J29/48 , B01J29/85 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C07C6/126 , C07C2521/04 , C07C2523/24 , C07C2523/28 , C07C2523/40 , C07C2523/755 , C07C2529/18 , C07C2529/40 , C07C2529/84 , C07C2529/85 , Y02P20/52 , C07C15/08 , C07C15/06
摘要： The multiple zeolite catalyst is a catalytic composition used to convert C9+ alkylaromatic hydrocarbons to BTX, particularly commercially valuable xylenes. The catalyst is formed by mixing at least two zeolites selected from mordenite, beta zeolite, ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, MFI topology zeolite, NES topology zeolite, EU-1, MAPO-36, SAPO-5, SAPO-11, SAPO-34, and SAPO-41, and adding at least one metal component selected from Group VIB and Group VIII of the Periodic Table of the Elements. The two zeolites should have different physical and chemical characteristics, such as pore size and acidity. An exemplary catalyst includes mordenite, ZSM-5, and 3 wt. % molybdenum. The transalkylation reaction may be conducted in one or more reactors with a fixed bed, moving bed, or radial flow reactor at 200-540° C., a pressure of 1.0-5.0 MPa, and liquid hourly space velocity of 1.0-5.0 per hour.
摘要翻译：多重沸石催化剂是用于将C 9+烷基芳族烃转化成BTX的催化组合物，特别是商业上有价值的二甲苯。催化剂是通过混合至少两种选自丝光沸石，β沸石，ZSM-5，ZSM-11，ZSM-12，ZSM-22，ZSM-23，MFI拓扑沸石，NES拓扑沸石，EU-1，MAPO -36，SAPO-5，SAPO-11，SAPO-34和SAPO-41，并加入至少一种选自元素周期表的VIB族和VIII族的金属组分。两种沸石应具有不同的物理和化学特性，如孔径和酸度。示例性催化剂包括丝光沸石，ZSM-5和3wt。％钼。烷基转移反应可以在固定床，移动床或径向流动反应器的一个或多个反应器中在200-540℃，压力为1.0-5.0MPa，液时空速为1.0-5.0 /小时。

4. 发明授权

US5338707A Process for production of high-purity mullites 失效
标题翻译：生产高纯度莫来石的方法
公开(公告)号：US5338707A
公开(公告)日：1994-08-16
申请号：US886551
申请日：1992-05-20
申请人： Tomoyuki Inui , Masashi Inoue
发明人： Tomoyuki Inui , Masashi Inoue
IPC分类号： C04B35/18 , C01B33/26 , C04B35/10 , C04B35/185 , C03C3/00
CPC分类号： C04B35/185 , C01B33/26
摘要： A process is disclosed for the production of high purity mullites. The process involves reacting a mixture of aluminum alkoxide and silicon alkoxide with an atomic ratio (weight) of Al/Si in the range of 2-7 in an aromatic hydrocarbon solvent at a temperature of 200.degree.-350.degree. C. and calcining the resulting reaction product at a temperature above 900.degree. C. The mullite product obtained finds wide application as a high temperature service structural material such as for automotive engines and turbines as well as a support for combustion catalyst.
摘要翻译：公开了用于生产高纯度莫来石的方法。该方法包括在200-350℃的温度下，使芳族烃溶剂中的铝/醇铝混合物与Al / Si的原子比（重量）在2-7范围内反应，并煅烧所得到的反应产物在高于900℃的温度下获得。所得到的莫来石产品作为高温服务结构材料，例如用于汽车发动机和涡轮机以及用于燃烧催化剂的支撑物被广泛应用。

5. 发明授权

US4400328A Crystalline aluminosilicate zeolite catalyst and the method for manufacturing thereof 失效
标题翻译：结晶硅铝酸盐沸石催化剂及其制造方法
公开(公告)号：US4400328A
公开(公告)日：1983-08-23
申请号：US312496
申请日：1981-10-19
申请人： Yoshinobu Takegami , Tomoyuki Inui , Takayuki Ishihara , Eiichi Araki , Toshihiro Kanie
发明人： Yoshinobu Takegami , Tomoyuki Inui , Takayuki Ishihara , Eiichi Araki , Toshihiro Kanie
IPC分类号： B01J29/70 , C01B39/30 , C07F5/06
CPC分类号： C01B39/305 , B01J29/70
摘要： The present invention relates to provide new crystalline zeolite catalyst (ZKU-catalyst) having the superior catalytic activity and selectivity and the long period of the catalytic life.One of the method of said catalyst (ZKU-2 catalyst) lies in crystallizing the starting zeolite preparation in the presence of the crystallization conditioning agent of crystallization of tetraalkyl (methyl or ethyl or combination thereof) ammonium cation.Another method of said catalyst (ZKU-3, 4 catalysts) lies in crystallizing the starting zeolite preparation in the presence of both said conditioning agent of crystallization and the substance capable of forming the seed and/or the skelton of crystal. The ZKU-3 catalyst is manufactured using the seed of crystal, while the ZKU-4 catalyst is manufactured using the seed and the skelton of crystal.The seed of crystal is useful for the promoter of the crystallization rate and the improvement of the catalytic activity, the skelton of crystal is useful for so-called "skelton" which is of use for the improvement of the mechanical strength, the dimentional stability and the conditioning of the pore structure of crystal in the molded catalyst and also for the improvement of uniformly dispersing the components of the catalytic composition.The characteristic feature of the ZKU-2, 3 and 4 catalysts of the present invention has been compared with that of the ZSM-34 catalyst.
摘要翻译：本发明涉及提供具有优异的催化活性和选择性以及长期催化寿命的新型结晶沸石催化剂（ZKU-催化剂）。所述催化剂（ZKU-2催化剂）的方法之一在于在四烷基（甲基或乙基或其组合）铵阳离子结晶的结晶调节剂存在下使起始沸石制剂结晶。所述催化剂（ZKU-3,4催化剂）的另一种方法在于在所述结晶调理剂和能够形成晶种的物质和/或晶体的晶体存在下，使起始沸石制剂结晶。 ZKU-3催化剂使用晶体晶种制造，而ZKU-4催化剂使用晶种和晶体晶体制造。晶体种子对于结晶速率的促进剂和催化活性的提高是有用的，晶体的碳化硅可用于所谓的“skelton”，其用于改善机械强度，尺寸稳定性和调节成型催化剂中晶体的孔结构，以及改进均匀分散催化剂组合物的组分。本发明的ZKU-2,3和4催化剂的特征与ZSM-34催化剂的特征进行了比较。

6. 发明申请

US20100240522A1 Catalyst exhibiting hydrogen spillover effect 审中-公开
标题翻译：催化剂表现出氢气溢出效应
公开(公告)号：US20100240522A1
公开(公告)日：2010-09-23
申请号：US12382737
申请日：2009-03-23
申请人： Tomoyuki Inui , Masayuki Inui , Takuma Kimura , Mohammad Abdullah Al-Saleh , Halim Hamid Redhwi , Mohammad Ashraf Ali , Shakeel Ahmed
发明人： Tomoyuki Inui , Masayuki Inui , Takuma Kimura , Mohammad Abdullah Al-Saleh , Halim Hamid Redhwi , Mohammad Ashraf Ali , Shakeel Ahmed
IPC分类号： B01J37/30 , B01J21/16
CPC分类号： B01J37/0201 , B01J21/16 , B01J23/652 , B01J23/89 , B01J23/8913 , B01J35/1019 , B01J35/1023 , B01J35/1038 , B01J35/1042 , B01J37/0205 , B01J37/18 , C10G29/205 , C10G45/10 , C10G47/14
摘要： The catalyst exhibiting hydrogen spillover effect relates to the composition of a catalyst exhibiting hydrogen spillover effect and to a process for preparing the catalyst. The catalyst has a reduced transition base metal of Group VIB or Group VIIIB, such as cobalt, nickel, molybdenum or tungsten, supported on a high porous carrier, such as saponite, the base metal being ion-exchanged with at least one precious metal of Group VIIIB. The process includes the steps of loading the base metal onto the support, reducing the base metal, preferably with H2 at 600° C., and thereafter ion-exchanging the precious metal with the base metal. Preferred examples of the catalyst include a saponite support loaded with about 10-20 wt % cobalt and about 0.1-1 wt % precious metal. The catalyst is optimized for reactions that occur in commercial processes at about 360-400° C., such as in hydrocracking.
摘要翻译：表现出氢气溢出效应的催化剂涉及显示氢气溢出效应的催化剂的组成和制备催化剂的方法。该催化剂具有负载在诸如皂石的高多孔载体上的VIB族或VIIIB族的钌基过渡金属，例如钴，镍，钼或钨，贱金属与至少一种贵金属离子交换第VIIIB组。该方法包括以下步骤：将贱金属加载到载体上，优选在600℃下用H 2还原贱金属，然后将贵金属与贱金属进行离子交换。催化剂的优选实例包括负载有约10-20重量％钴和约0.1-1重量％贵金属的皂石载体。该催化剂针对在约360-400℃的商业过程中发生的反应进行优化，例如在加氢裂化中。

7. 发明授权

US5393793A Oxide-based catalyst, production thereof, and catalytic hydrogenation of CO.sub.2 using said catalyst 失效
标题翻译：使用所述催化剂的氧化物基催化剂，其生产和CO 2的催化氢化
公开(公告)号：US5393793A
公开(公告)日：1995-02-28
申请号：US39229
申请日：1993-04-19
申请人： Tomoyuki Inui
发明人： Tomoyuki Inui
IPC分类号： B01J23/80 , B01J23/83 , B01J23/86 , B01J37/04 , C07B61/00 , C07C29/154 , C07C31/04 , C07C27/06 , B01J23/10
CPC分类号： C07C29/154 , B01J23/80 , B01J23/83 , B01J23/868 , B01J37/04 , Y02P20/52
摘要： A compound oxide X.sub.1 having the oxide composition CuO-ZnO-Cr.sub.2 O.sub.3 -Al.sub.2 O.sub.3 is physically admixed with a compound oxide X.sub.2 prepared by impregnating .gamma.-Al.sub.2 O.sub.3 with La(NO.sub.3).sub.3 and firing the same, to give a CuO-ZnO-Cr.sub.2 O.sub.3 -Al.sub.2 O.sub.3 -La.sub.2 O.sub.3 -based compound oxide with an La.sub.2 O.sub.3 addition level of 4% by weight. This compound oxide is reduced and packed into a reactor and a mixed gas composed of CO.sub.2 and H.sub.2 in a mole ratio of 1:3 is fed to the reactor, whereby methanol is obtained in high yield. The total conversion of CO.sub.2 amounts to 31.0%, the conversion to methanol being 22.9% (selectivity toward methanol 73.9%). When the pressure is 80 atmospheres, the conversion of CO.sub.2 amounts to 39%, the conversion to methanol being 29%.
摘要翻译： PCT No.PCT / JP92 / 01039 Sec。 371日期：1993年4月19日 102（e）日期1993年4月19日PCT提交1992年8月17日PCT公布。出版物WO93 / 03837 日期为1993年3月4日。具有氧化物组成为CuO-ZnO-Cr2O3-Al2O3的复合氧化物X1与通过用La（NO 3）3浸渍γ-Al 2 O 3并制备的复合氧化物X2物理混合， CuO-ZnO-Cr2O3-Al2O3-La2O3基复合氧化物，La2O3添加量为4重量％。将该复合氧化物还原并填充到反应器中，将由CO 2和H 2组成的摩尔比为1:3的混合气体进料到反应器中，从而以高产率获得甲醇。 CO 2的总转化率为31.0％，转化为甲醇为22.9％（对甲醇的选择性为73.9％）。当压力为80个大气压时，CO 2的转化率为39％，甲醇的转化率为29％。

8. 发明授权

US4705907A Production of liquid hydrocarbon from gas containing lower hydrocarbon 失效
标题翻译：从含有低碳氢化合物的气体生产液态烃
公开(公告)号：US4705907A
公开(公告)日：1987-11-10
申请号：US864779
申请日：1986-05-19
申请人： Tomoyuki Inui
发明人： Tomoyuki Inui
IPC分类号： B01J29/00 , B01J29/04 , B01J29/48 , B01J29/70 , B01J29/86 , B01J29/87 , B01J29/88 , B01J29/89 , C07C2/00 , C10G50/00 , C10G57/02
CPC分类号： C07C2/00 , B01J29/04 , B01J29/70 , C07C2521/16 , C07C2529/04
摘要： Liquid hydrocarbon is prepared with high efficiency from hydrocarbon gas containing C.sub.2 -C.sub.5 paraffinic hydrocarbons and/or C.sub.2 -C.sub.5 olefinic hydrocarbons by bringing the gas into contact with a metallo-silicate catalyst having the following chemical composition in mol %:Si/Me:15-3500OH.sup.- /SiO.sub.2 :0.3-1.0H.sub.2 O/SiO.sub.2 :30-100R/(R+alkali metal):0.05-0.15NaCl/H.sub.2 O:0.01-0.06where R is quaternary alkylammonium cation,alkali metal is Na or K, Me is metal ion of B, Al, Ti, V, Cr, Mn, Fe, Co, Ni, Zn, Ga, Ge, Zr, Mo, W, La or Sc,and having the following acidity per g of catalyst:total acid 0.1-4.5 milli-equivalentstrong acid 0.05-2.0 milli-equivalentweak acid 0.05-3.0 milli-equivalent.
摘要翻译：通过使气体与具有以摩尔％计的以下化学组成的金属硅酸盐催化剂接触来制备含有C 2 -C 5链烷烃和/或C 2 -C 5烯烃的烃气体的液体烃：Si / Me：15 -3500 OH- / SiO 2：0.3-1.0H 2 O / SiO 2：30-100R /（R +碱金属）：0.05-0.15 NaCl / H 2 O：0.01-0.06其中R是季烷基铵阳离子，碱金属是Na或K， Me是B，Al，Ti，V，Cr，Mn，Fe，Co，Ni，Zn，Ga，Ge，Zr，Mo，W，La或Sc的金属离子，每g催化剂具有以下酸度：酸0.1-4.5毫当量强酸0.05-2.0毫当量弱酸0.05-3.0毫当量。

9. 发明授权

US4704494A Conversion process of aromatic hydrocarbon from low molecular paraffin hydrocarbon 失效
标题翻译：芳烃从低分子链烷烃转化过程
公开(公告)号：US4704494A
公开(公告)日：1987-11-03
申请号：US22561
申请日：1987-03-04
申请人： Tomoyuki Inui
发明人： Tomoyuki Inui
IPC分类号： C07C2/76 , B01J21/06 , B01J23/08 , B01J23/42 , B01J23/56 , B01J23/89 , B01J29/00 , B01J29/04 , B01J29/06 , B01J29/068 , C07B61/00 , C07C1/00 , C07C2/00 , C07C15/02 , C07C67/00 , C10G35/06 , C10G35/085 , C10G35/095 , C07C2/52
CPC分类号： B01J23/89 , B01J21/06 , B01J23/08 , B01J23/42 , B01J23/56 , C07C2/00 , C07C2529/04
摘要： Low molecular paraffin hydrocarbons can be converted to aromatic hydrocarbons at high yields of 20-30% in the presence of a metallo-silicate catalyst (Si/Me) (wherein atomic ratio of Si/Me is 25-3200 and Me is Al, Ga, Ti, Zr, Ge, La, Mn, Cr, Sc, V, Fe, W, Mo or Ni) modified with 0.25-1.5% by weight of platinum or gallium or a gallium-silicate catalyst (atomic ratio of Si/Ga is 25-3200).Since said catalyst is of high activity and reaction is carried out at low temperatures, reduction of selectivity of the catalyst caused by decomposition of aromatic hydrocarbons produced can be prevented.
摘要翻译：在金属硅酸盐催化剂（Si / Me）（Si / Me原子比为25-3200，Me为Al，Ga的原子比为25-3200）的情况下，低分子链烷烃可以以20-30％的高收率转化为芳烃，由0.25-1.5重量％的铂或镓或硅酸镓催化剂（Si / Ga的原子比）修饰的Ti，Zr，Ge，La，Mn，Cr，Sc，V，Fe，W，Mo或Ni）是25-3200）。由于所述催化剂具有高活性并且在低温下进行反应，因此可以防止由所产生的芳族烃的分解引起的催化剂选择性的降低。

10. 发明申请

US20100029467A1 Multiple zeolite catalyst 审中-公开
标题翻译：多重沸石催化剂
公开(公告)号：US20100029467A1
公开(公告)日：2010-02-04
申请号：US12219927
申请日：2008-07-30
申请人： Tomoyuki Inui , Masayuki Inui , Mohammad A. Ali , Muhammad A. Al-Saleh , Syed A. Ali , Khalid Al-Nawad , Tsutomu Okamoto , Katsuhiko Ishikawa , Minoru Hatayama
发明人： Tomoyuki Inui , Masayuki Inui , Mohammad A. Ali , Muhammad A. Al-Saleh , Syed A. Ali , Khalid Al-Nawad , Tsutomu Okamoto , Katsuhiko Ishikawa , Minoru Hatayama
IPC分类号： B01J29/46 , B01J29/072 , B01J29/48 , B01J29/26 , B01J29/076 , B01J29/24 , B01J29/40
CPC分类号： B01J29/80 , B01J29/005 , B01J29/061 , B01J29/064 , B01J29/076 , B01J29/18 , B01J29/26 , B01J29/40 , B01J29/48 , B01J29/85 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C07C6/126 , C07C2521/04 , C07C2523/24 , C07C2523/28 , C07C2523/40 , C07C2523/755 , C07C2529/18 , C07C2529/40 , C07C2529/84 , C07C2529/85 , Y02P20/52 , C07C15/08 , C07C15/06
摘要： The multiple zeolite catalyst is a catalytic composition used to convert C9+ alkylaromatic hydrocarbons to BTX, particularly commercially valuable xylenes. The catalyst is formed by mixing at least two zeolites selected from mordenite, beta zeolite, ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, MFI topology zeolite, NES topology zeolite, EU-1, MAPO-36, SAPO-5, SAPO-11, SAPO-34, and SAPO-41, and adding at least one metal component selected from Group VIB and Group VIII of the Periodic Table of the Elements. The two zeolites should have different physical and chemical characteristics, such as pore size and acidity. An exemplary catalyst includes mordenite, ZSM-5, and 3 wt. % molybdenum. The transalkylation reaction may be conducted in one or more reactors with a fixed bed, moving bed, or radial flow reactor at 200-540° C., a pressure of 1.0-5.0 MPa, and liquid hourly space velocity of 1.0-5.0 per hour.
摘要翻译：多重沸石催化剂是用于将C 9+烷基芳族烃转化成BTX的催化组合物，特别是商业上有价值的二甲苯。催化剂是通过混合至少两种选自丝光沸石，β沸石，ZSM-5，ZSM-11，ZSM-12，ZSM-22，ZSM-23，MFI拓扑沸石，NES拓扑沸石，EU-1，MAPO -36，SAPO-5，SAPO-11，SAPO-34和SAPO-41，并加入至少一种选自元素周期表的VIB族和VIII族的金属组分。两种沸石应具有不同的物理和化学特性，如孔径和酸度。示例性催化剂包括丝光沸石，ZSM-5和3wt。％钼。烷基转移反应可以在固定床，移动床或径向流动反应器的一个或多个反应器中在200-540℃，压力为1.0-5.0MPa，液时空速为1.0-5.0 /小时。

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