公开(公告)号：US20110207984A1

公开(公告)日：2011-08-25

申请号：US13059377

申请日：2009-09-18

Applicant: Marlon Brando Bezerra De Almeida ,  Alexandre de Figueiredo Costa ,  Lam Yiu Lau ,  Sergio Augusto Santos Rodrigues ,  Marcelo Andre Torem

Inventor： Marlon Brando Bezerra De Almeida ,  Alexandre de Figueiredo Costa ,  Lam Yiu Lau ,  Sergio Augusto Santos Rodrigues ,  Marcelo Andre Torem

IPC: C07C4/06 ,  B01J29/80 ,  B01J37/04 ,  B01J37/08 ,  B01J37/06

CPC classification number: C10G11/18 ,  B01J29/084 ,  B01J29/40 ,  B01J29/80 ,  B01J35/023 ,  B01J35/1014 ,  B01J35/1061 ,  B01J35/1066 ,  B01J37/0009 ,  B01J37/0045 ,  B01J37/04 ,  B01J37/28 ,  B01J2229/42 ,  C10G2400/20

Abstract: Additives for mixing with the catalyst inventory in process units for fluid catalytic cracking (FCC) for maximizing the production of LPG and light olefins are described. Said additives comprise a matrix that incorporates a zeolite of type MFI, preferably zeolite ZSM-5, a zeolite of type Y, and a source of phosphorus, in a single particle. Mixing of the additive in proportions from 1.0 to 40 wt. % with the equilibrium catalyst of an FCC unit maximizes the production of LPG and light olefins, chiefly propylene.

Abstract translation: 描述了用于与催化剂库存混合用于流化催化裂化（FCC）的用于最大化LPG和轻质烯烃生产的流化催化裂化的添加剂。 所述添加剂包括在单个颗粒中掺入MFI沸石，优选沸石ZSM-5，Y型沸石和磷源的基质。 混合添加剂的比例为1.0〜40wt。 与FCC装置的平衡催化剂的％最大化LPG和轻质烯烃的生产，主要是丙烯。

公开(公告)号：US20110189069A1

公开(公告)日：2011-08-04

申请号：US13086857

申请日：2011-04-14

Applicant: Yasuyoshi KATO ,  Keiichiro KAI ,  Naomi IMADA

Inventor： Yasuyoshi KATO ,  Keiichiro KAI ,  Naomi IMADA

IPC: B01D53/56 ,  B01D53/64

CPC classification number: B01J23/31 ,  B01D53/8665 ,  B01D2251/2062 ,  B01D2255/20707 ,  B01D2255/20723 ,  B01D2255/20769 ,  B01D2255/20776 ,  B01D2257/404 ,  B01D2257/602 ,  B01J23/002 ,  B01J23/28 ,  B01J23/30 ,  B01J27/199 ,  B01J35/06 ,  B01J37/28 ,  B01J2523/00 ,  B01J2523/47 ,  B01J2523/54 ,  B01J2523/55 ,  B01J2523/69 ,  B01J2523/68

Abstract: The invention realizes a catalyst which is hardly deteriorated even when volatile catalyst-poisoning compounds such as P and As are accumulated and which can reduce the rate of oxidation of SO2 to a level as low as a fraction of that of the catalyst in the prior art, and provides an exhaust gas purification catalyst which can maintain a high activity and a low rate of oxidation of SO2 for a long time even with any diversified coal, a method of producing the same, and an exhaust gas purification method using the same. Disclosed is an exhaust gas purification catalyst having a composition comprising oxides of titanium (Ti), molybdenum (Mo) and/or tungsten (W), vanadium (V) and bismuth (Bi), wherein the atomic ratio of Ti:(Mo and/or W):V is 75 to 98.9:1 to 0.1 to 10 and the atomic ratio of Bi/(Mo and/or W) is 0.1 to 0.8.

Abstract translation: 本发明实现了即使当诸如P和As等挥发性催化剂中毒化合物被累积并且可以将SO 2的氧化速率降低到现有技术中的催化剂的一部分的程度时也几乎不劣化的催化剂 并且提供了即使使用任何多种煤也能长时间保持SO 2的高活性和低氧化率的废气净化催化剂，其制造方法和使用该废气净化催化剂的废气净化方法。 公开了具有钛（Ti），钼（Mo）和/或钨（W），钒（V）和铋（Bi）的氧化物的组成的废气净化催化剂，其中Ti：（Mo和 /或W）：V为75〜98.9:1〜0.1〜10，Bi /（Mo和/或W）的原子比为0.1〜0.8。

公开(公告)号：US07883806B2

公开(公告)日：2011-02-08

申请号：US12380163

申请日：2009-02-23

Applicant: Leonid Gorobinskiy ,  Norboru Sato ,  Ju-Yong Kim ,  Myoung-Ki Min ,  Jin-Goo Ahn ,  Elena Alekseeva

Inventor： Leonid Gorobinskiy ,  Norboru Sato ,  Ju-Yong Kim ,  Myoung-Ki Min ,  Jin-Goo Ahn ,  Elena Alekseeva

IPC: H01M8/06 ,  B01J27/043 ,  B01J27/045 ,  B01J23/10

CPC classification number: B01J37/0201 ,  B01J21/066 ,  B01J23/63 ,  B01J37/20 ,  B01J37/28 ,  H01M8/0631 ,  Y02P70/56

Abstract: A fuel cell reforming catalyst includes a platinum-group metal; an inorganic oxide selected from CeO2, Pr6O11, and combinations thereof; a strong acid ion; and a carrier. The fuel cell reforming catalyst has high activity for the reforming reaction at low temperatures and low space velocities.

Abstract translation: 燃料电池重整催化剂包括铂族金属; 选自CeO 2，Pr 6 O 11的无机氧化物及其组合; 强酸离子; 和载体。 燃料电池重整催化剂在低温下的重整反应活性高，空速低。

公开(公告)号：US07879224B2

公开(公告)日：2011-02-01

申请号：US11663497

申请日：2005-09-20

Applicant: Patrick Euzen ,  Alexandra Chaumonnot ,  Magalie Roy-Auberger ,  Patrick Bourges ,  Tivadar Cseri ,  Maryline Delage ,  Nathalie Lett

Inventor： Patrick Euzen ,  Alexandra Chaumonnot ,  Magalie Roy-Auberger ,  Patrick Bourges ,  Tivadar Cseri ,  Maryline Delage ,  Nathalie Lett

IPC: C10G11/02 ,  B01J27/185

CPC classification number: B01J21/12 ,  B01J21/02 ,  B01J23/883 ,  B01J23/888 ,  B01J27/1853 ,  B01J27/188 ,  B01J35/0006 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/108 ,  B01J37/0201 ,  B01J37/20 ,  B01J37/28 ,  C10G49/02 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/4018

Abstract: The present invention concerns doped catalysts on an alumino-silicate support with an adapted macropore content and hydrocracking/hydroconversion and hydrotreatment processes employing them. The catalyst comprises at least one hydrodehydrogenating element selected from the group formed by elements from group VIB and group VIII of the periodic table, a controlled quantity of phosphorus (optionally in combination with boron and/or silicon) as a doping element, and a non-zeolitic support based on alumina-silica containing a quantity of more than 5% by weight and 95% by weight or less of silica (SiO2).

Abstract translation: 本发明涉及具有适用的大孔含量和加氢裂化/加氢转化和使用它们的加氢处理方法的铝硅酸盐载体上的掺杂催化剂。 该催化剂包含至少一种选自元素周期表第VIB族和第VIII族的元素形成的氢化脱氢元素，受控量的磷（任选与硼和/或硅组合）作为掺杂元素， - 基于含有大于5重量％和95重量％或更少的二氧化硅（SiO 2）的量的氧化铝 - 二氧化硅的硅铝石载体。

公开(公告)号：US20100322832A1

公开(公告)日：2010-12-23

申请号：US12866328

申请日：2009-02-19

Applicant: Jan Procházka, JR. ,  Jan Procházka, SR.

Inventor： Jan Procházka, JR. ,  Jan Procházka, SR.

IPC: B01D53/94 ,  B01J21/06

CPC classification number: B01J21/063 ,  B01D2255/10 ,  B01D2255/20707 ,  B01D2255/802 ,  B01J23/28 ,  B01J23/40 ,  B01J23/42 ,  B01J23/50 ,  B01J23/52 ,  B01J23/72 ,  B01J23/755 ,  B01J35/004 ,  B01J35/006 ,  B01J35/023 ,  B01J35/1014 ,  B01J37/28 ,  B82Y30/00 ,  C01G23/0532 ,  C01P2002/54 ,  C01P2004/03 ,  C01P2004/50 ,  C01P2004/64 ,  C01P2004/90 ,  C01P2006/12

Abstract: The TiO2 catalyst structure consisting of TiO2 nano-particles in the anatase crystal form, doped with 0.05-5 wt % phosphorus on the TiO2 basis, organized in the circular planar aggregates with the specific surface area ranging from 40 to 120 m2/g, suitable for catalytic processes at the temperature up to 800° C., and the TiO2 catalyst structure of with the morphology of the aggregated compact particles, with the specific surface area from 20 to 40 m2/g, suitable for the catalytic processes at the temperature up to 1000° C. Active substances selected from the group consisting of silver, copper, gold, platinum metals, nickel, molybdenum and metal oxides except for alkaline metals oxides can be applied onto the surface of both types of the structure.

Abstract translation: TiO 2催化剂结构由锐钛型晶体形式的TiO 2纳米颗粒组成，掺杂有基于TiO2的0.05-5重量％的磷，组织在比表面积为40至120m 2 / g的圆形平面聚集体中，合适的 用于在高达800℃的温度下的催化过程，并且具有聚集的致密颗粒的形态的TiO 2催化剂结构，比表面积为20至40m 2 / g，适于在升温时的催化过程 选自银，铜，金，铂金属，镍，钼和除了碱金属氧化物以外的金属氧化物的活性物质可以施加到两种类型的结构的表面上。

公开(公告)号：US20100261940A1

公开(公告)日：2010-10-14

申请号：US12739217

申请日：2008-09-22

Applicant: Ki-Won Jun ,  Yun-Jo Lee ,  Jong-Wook Bae ,  Jo Yong Park

Inventor： Ki-Won Jun ,  Yun-Jo Lee ,  Jong-Wook Bae ,  Jo Yong Park

IPC: C07C1/04

CPC classification number: C07C1/044 ,  B01J23/002 ,  B01J23/745 ,  B01J23/78 ,  B01J23/80 ,  B01J23/8472 ,  B01J23/862 ,  B01J23/8892 ,  B01J29/40 ,  B01J29/405 ,  B01J37/031 ,  B01J37/18 ,  B01J37/28 ,  B01J2229/186 ,  B01J2523/00 ,  C10G2/32 ,  C10G2/332 ,  C10G2400/20 ,  Y02P20/588 ,  C07C11/02 ,  B01J2523/17 ,  B01J2523/31 ,  B01J2523/842 ,  B01J2523/13

Abstract: The present invention relates to a process for producing light olefins from a synthesis gas with significantly improved conversion and selectivity for C2-C4 light olefins in general and propylene in particular, as compared to a conventional process, through a sequential two-step process comprising preparing olefin compounds from a synthesis gas in the presence of an iron catalyst by the Fischer-Tropsch reaction followed by cracking the olefin compounds in the presence of a zeolite catalyst.

Abstract translation: 本发明涉及一种从合成气中生产轻质烯烃的方法，通常通过连续的两步方法，通过顺序的两步方法，其制备方法特别是与常规方法相比，具有显着提高的C 2 -C 4轻质烯烃的转化率和选择性，特别是丙烯 烯烃化合物在铁催化剂存在下通过费 - 托反应，然后在沸石催化剂存在下裂解烯烃化合物。

公开(公告)号：US07811961B2

公开(公告)日：2010-10-12

申请号：US11539722

申请日：2006-10-09

Applicant: Hungwen Jen ,  George Graham ,  Robert McCabe

Inventor： Hungwen Jen ,  George Graham ,  Robert McCabe

IPC: B01J23/00 ,  B01J21/00 ,  B01J20/00 ,  B01J29/00 ,  B01J37/00

CPC classification number: B01J37/0207 ,  B01D53/9418 ,  B01D2255/911 ,  B01J27/185 ,  B01J37/28 ,  Y02A50/2325

Abstract: According to one embodiment of the present invention, an enhanced NH3 adsorbing automotive exhaust composition including a catalyst composition suitable for use in a selective catalytic reduction (SCR) system and an acidified support composition for enhancing NH3 adsorption capacity of the automotive exhaust composition is disclosed.

Abstract translation: 根据本发明的一个实施方案，公开了包含适用于选择性催化还原（SCR）系统的催化剂组合物和用于增强汽车排气组合物的NH 3吸附能力的酸化载体组合物的增强型NH 3吸附汽车排气组合物。

公开(公告)号：US20100243530A1

公开(公告)日：2010-09-30

申请号：US12666694

申请日：2008-06-03

Applicant: Karin Marchand ,  Mathieu Digne

Inventor： Karin Marchand ,  Mathieu Digne

IPC: C10G45/00 ,  B01J27/188 ,  B01J27/19 ,  C10G45/34

CPC classification number: B01J27/1853 ,  B01J21/04 ,  B01J23/882 ,  B01J23/883 ,  B01J27/188 ,  B01J27/19 ,  B01J31/0258 ,  B01J37/0203 ,  B01J37/0205 ,  B01J37/20 ,  B01J37/28 ,  C10G49/04 ,  C10G2300/1081 ,  C10G2300/1088 ,  C10G2300/1096 ,  C10G2300/44

Abstract: The invention concerns a process for preparing a hydrotreatment catalyst, comprising the following steps: a) at least one step for impregnation of a calcined and/or dried catalytic precursor containing at least one element from group VIII and/or at least one element from group VIB and an amorphous support, using an impregnation solution constituted by at least one phosphorus-containing compound in solution in at least one polar solvent with a dielectric constant of more than 20; b) a step for maturing said impregnated catalytic precursor from step a); c) a step for drying, without a subsequent calcining step, said catalytic precursor from step b).

Abstract translation: 本发明涉及一种制备加氢处理催化剂的方法，包括以下步骤：a）至少一个步骤，用于浸渍含有VIII族中至少一种元素的煅烧和/或干燥的催化前体和/或至少一种元素， VIB和无定形载体，使用在至少一种介电常数大于20的极性溶剂中的溶液中由至少一种含磷化合物构成的浸渍溶液; b）从步骤a）成熟所述浸渍的催化前体的步骤; c）在步骤b）中，无需随后的煅烧步骤干燥所述催化前体的步骤。

公开(公告)号：US20100093523A1

公开(公告)日：2010-04-15

申请号：US12594617

申请日：2008-01-30

Applicant: Ki-won Jun ,  Jong-Wook Bae ,  Seung-Moon Kim ,  Yun-Jo Lee

Inventor： Ki-won Jun ,  Jong-Wook Bae ,  Seung-Moon Kim ,  Yun-Jo Lee

IPC: B01J27/185

CPC classification number: B01J23/75 ,  B01J27/16 ,  B01J27/1853 ,  B01J35/10 ,  B01J35/1019 ,  B01J35/1023 ,  B01J35/109 ,  B01J37/0201 ,  B01J37/0207 ,  B01J37/033 ,  B01J37/18 ,  B01J37/28

Abstract: The present invention relates to a cobalt/phosphorus-alumina catalyst in which cobalt is supported as an active component on a phosphorus-alumina support wherein phosphorus is supported on alumina surface. With a bimodal pore structure of pores of relatively different pore sizes, the catalyst provides superior heat- and matter-transfer performance and excellent catalytic reactivity. Especially, when Fischer-Tropsch (F-T) reaction is performed using the catalyst, deactivation by the water produced during the F-T reaction is inhibited and, at the same time, the dispersion and reducing property of cobalt and other active component are improved. Therefore, the cobalt/phosphorus-alumina catalyst for F-T reaction in accordance with the present invention provides good carbon monoxide conversion and stable selectivity for liquid hydrocarbons.

Abstract translation: 本发明涉及一种钴/磷 - 氧化铝催化剂，其中钴作为活性组分负载在磷 - 氧化铝载体上，其中磷负载在氧化铝表面上。 具有相对不同孔径的孔的双峰孔结构，催化剂提供优异的热和物质转移性能和优异的催化反应性。 特别是当使用催化剂进行费托（F-T）反应时，抑制了F-T反应期间产生的水的失活，同时改善了钴等活性成分的分散还原性。 因此，根据本发明的用于F-T反应的钴/磷 - 氧化铝催化剂提供了良好的一氧化碳转化率和对液体烃的稳定选择性。

公开(公告)号：US20090275788A1

公开(公告)日：2009-11-05

申请号：US12447096

申请日：2007-11-09

Applicant: Robert L Bedard ,  Jeffery C. Bricker ,  Dean E. Rende ,  Ally S. Chan

Inventor： Robert L Bedard ,  Jeffery C. Bricker ,  Dean E. Rende ,  Ally S. Chan

IPC: C07C5/10

CPC classification number: B01J21/08 ,  B01J21/12 ,  B01J23/26 ,  B01J23/30 ,  B01J23/32 ,  B01J23/40 ,  B01J23/42 ,  B01J23/44 ,  B01J23/48 ,  B01J23/72 ,  B01J23/74 ,  B01J23/75 ,  B01J27/185 ,  B01J35/002 ,  B01J35/0066 ,  B01J35/008 ,  B01J35/06 ,  B01J35/10 ,  B01J35/1009 ,  B01J37/0207 ,  B01J37/06 ,  B01J37/28 ,  B01J37/30 ,  C07C5/02 ,  C07C5/10 ,  C07C2521/12 ,  C07C2523/30 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/50 ,  C07C2523/72 ,  C07C2523/75 ,  C10G45/52 ,  C07C13/18

Abstract: Hydrogenation processes using a catalyst composition which, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous substrate has (i) a total surface area between about 0.01 m2/g and 10 m2/g; and (ii) a predetermined isoelectric point (IEP) obtained in a pH range greater than 0, preferably greater than or equal to 4.5, or more preferably greater than or equal to 6.0, but less than or equal to 14. At least one catalytically-active region may be contiguous or discontiguous and has a mean thickness less than or equal to about 30 nm, preferably less than or equal to 20 nm and more preferably less than or equal to 10 nm. Preferably, the substrate is a glass composition having a SARCNa less than or equal to about 0.5.

Abstract translation: 使用催化剂组合物的氢化方法，催化剂组合物优选包含玻璃基底，其中一个或多个功能性表面活性成分集成在基底表面上和/或基底表面。 基本上无孔基材具有（i）约0.01m 2 / g至10m 2 / g之间的总表面积; 和（ii）在大于0，优选大于或等于4.5，或更优选大于或等于6.0，但小于或等于14的pH范围内获得的预定等电点（IEP）。至少一种催化 活性区域可以是连续的或不连续的，并且具有小于或等于约30nm，优选小于或等于20nm，更优选小于或等于10nm的平均厚度。 优选地，基底是具有小于或等于约0.5的SARCNa的玻璃组合物。