公开(公告)号：WO2009121827A3

公开(公告)日：2010-04-01

申请号：PCT/EP2009053723

申请日：2009-03-30

Applicant: BASF SE ,  BOEHLING RALF ,  DECKERS ANDREAS ,  GRITSCH ACHIM ,  KOTREL STEFAN

Inventor： BOEHLING RALF ,  DECKERS ANDREAS ,  GRITSCH ACHIM ,  KOTREL STEFAN

IPC: C01C3/02 ,  B01J12/00 ,  B01J19/24

CPC classification number: C01C3/0204 ,  B01J19/0093 ,  B01J19/249 ,  B01J2219/00783 ,  B01J2219/00788 ,  B01J2219/00822 ,  B01J2219/00824 ,  B01J2219/00835 ,  B01J2219/0086 ,  B01J2219/00873 ,  B01J2219/00889 ,  B01J2219/2453 ,  B01J2219/2459 ,  B01J2219/2465 ,  B01J2219/2474 ,  B01J2219/2479 ,  B01J2219/2481 ,  B01J2219/2486 ,  B01J2219/2487 ,  B01J2219/2497 ,  C01C3/02

Abstract: Method for producing hydrogen cyanide through catalytic dehydration of gaseous formamide, wherein the dehydration of formamide is coupled with an exothermic reaction, in which the reactor used for dehydration comprises two separate fluid paths that are separated by a common reactor wall, wherein one fluid path is provided for the dehydration of formamide and the second fluid path is provided for the exothermic reaction.

Abstract translation: 一种通过气态甲酰胺的催化脱水，其中甲酰胺的脱水耦合通过在脱水中使用的反应器的放热反应制备氢氰酸的过程包括通过共同的反应器壁分开的两个独立的流体路径，其特征在于，一个用于脱水的流体路径 提供甲酰胺和被设置用于放热反应的第二流体路径。

公开(公告)号：WO2014203179A3

公开(公告)日：2015-06-25

申请号：PCT/IB2014062364

申请日：2014-06-18

Applicant: BASF SE ,  BASF CHINA CO LTD

Inventor： KÖNIG RENE ,  HANNEMANN STEFAN ,  KOBAN WIELAND ,  ARNOLD MIRKO ,  SUNDERMANN ANDREAS ,  SACHWEH BERND ,  FRANK KERSTIN ,  MAGES-SAUTER CAROLINE ,  KOTREL STEFAN

IPC: C01B13/34

CPC classification number: C01G25/02 ,  B01D53/944 ,  B01D53/945 ,  B01D2255/206 ,  B01D2255/2061 ,  B01D2255/2065 ,  B01D2255/20715 ,  B01D2255/908 ,  B01D2258/01 ,  B01J23/002 ,  B01J23/10 ,  B01J23/63 ,  B01J35/0013 ,  B01J35/1009 ,  B01J35/1014 ,  B01J37/0045 ,  B01J37/088 ,  B01J37/349 ,  B01J2523/00 ,  C01F17/0043 ,  C01G25/00 ,  C01P2002/50 ,  C01P2002/52 ,  C01P2004/51 ,  C01P2004/61 ,  C01P2004/62 ,  C01P2004/64 ,  C01P2006/12 ,  Y02T10/22 ,  B01J2523/3706 ,  B01J2523/3712 ,  B01J2523/3725 ,  B01J2523/48 ,  B01J2523/824

Abstract: A process for the production of mixed oxide particles comprising: (1) providing a dispersion comprising a disperse phase and a continuous phase, wherein the disperse phase comprises one or more precursor compounds of ceria, one or more precursor compounds of zirconia, and one or more precursor compounds of one or more rare earth oxides other than ceria and/or one or more precursor compounds of yttria; (2) forming an aerosol of the dispersion provided in step (1); and (3) pyrolyzing the aerosol of step (2) to obtain mixed oxide particles, as well as to mixed oxide particles obtainable from flame spray pyrolysis, and preferably obtainable by the process and to its use.

Abstract translation: 一种制备混合氧化物颗粒的方法，包括：（1）提供包含分散相和连续相的分散体，其中分散相包含一种或多种二氧化铈的前体化合物，一种或多种氧化锆的前体化合物，以及一种或多种 一种或多种除二氧化铈以外的稀土氧化物和/或一种或多种氧化钇前体化合物的前体化合物; （2）形成步骤（1）中提供的分散体的气溶胶; （3）热解步骤（2）的气溶胶以获得混合的氧化物颗粒，以及可由火焰喷雾热解获得的混合氧化物颗粒，并且优选可通过该方法获得和使用。

公开(公告)号：WO2009037281A3

公开(公告)日：2010-03-25

申请号：PCT/EP2008062375

申请日：2008-09-17

Applicant: BASF SE ,  KOTREL STEFAN ,  EMMELUTH MARIO ,  BENOEHR ALEXANDER

Inventor： KOTREL STEFAN ,  EMMELUTH MARIO ,  BENOEHR ALEXANDER

IPC: C10G1/08

CPC classification number: C10G1/083 ,  B01J27/22 ,  C10G3/44 ,  C10G3/45 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/44 ,  Y02P30/20

Abstract: The present invention relates to a single-stage method for the hydrogenating separation of lignin using a catalyst comprising a transition metal carbide, optionally in mixture with additional catalysts, comprising the following steps: (A) mixing the catalyst or the catalyst mixture with lignin in at least one organic solvent; (B) conversion of the mixture from (A) with hydrogen; (C) separation of the reaction products.

Abstract translation: 本发明涉及一种一步法的木质素在一个含过渡金属的催化剂的加氢裂解，任选地与其它催化剂的混合物，其包括以下步骤：（A）将催化剂或与至少一种有机溶剂木质素的催化剂混合物; （B）的（A）与氢气的混合物反应; （C）中分离出反应产物。

公开(公告)号：NZ588218A

公开(公告)日：2012-02-24

申请号：NZ58821809

申请日：2009-03-30

Applicant: BASF SE

Inventor： BOEHLING RALF ,  DECKERS ANDREAS ,  GRITSCH ACHIM ,  KOTREL STEFAN

IPC: C01C3/02 ,  B01J12/00 ,  B01J19/24

Abstract: Disclosed is a process for preparing hydrocyanic acid by catalytic dehydration of gaseous formamide at temperatures of from 350 to 650 degrees C in a reactor, wherein the dehydration of formamide is coupled with an exothermic reaction by the reactor comprising two separate fluid paths which are separated by a common reactor wall, with one fluid path being provided for the dehydration of formamide and the second fluid path being provided for the exothermic reaction and the common reactor wall being made of a material having a specific thermal conductivity lambda of at least 10 W/(mK), wherein the exothermic reaction is a catalytic combustion of combustible gases with introduction of oxygen.

公开(公告)号：DE102008002535A1

公开(公告)日：2009-01-02

申请号：DE102008002535

申请日：2008-06-19

Applicant: BASF SE

Inventor： CHIN SOO YIN ,  JOHANN THORSTEN ,  KOTREL STEFAN ,  GUMLICH KAI ,  TELES JOAQUIM HENRIQUE ,  WEYRAUCH JAN PHILLIPP ,  DELLA PINA CRISTINA ,  FALLETTA ERMELINDA ,  ROSSI MICHELE

IPC: C07C45/37 ,  B01J23/48 ,  C07C45/38 ,  C07C45/39 ,  C07C47/127

Abstract: Producing vicinal dioxo compounds, which exhibit a boiling point of = to the reaction temperature at reaction pressure, comprises heterogeneously catalyzed gas phase oxidation of the corresponding vicinal dihydroxy compounds, which exhibit a boiling point of = to the reaction temperature at reaction pressure, in the presence of gases containing oxygen on a catalyst comprising silver as active component and optionally gold, at a reaction temperature of 200-450[deg] C and a reaction pressure of 0.01-1 MPa. Producing vicinal dioxo compounds, which exhibit a boiling point of = to the reaction temperature at reaction pressure, comprises heterogeneously catalyzed gas phase oxidation of the corresponding vicinal dihydroxy compounds, which exhibit a boiling point of = to the reaction temperature at reaction pressure, in the presence of gases containing oxygen on a catalyst comprising silver as active component and optionally gold, at a reaction temperature of 200-450[deg] C and a reaction pressure of 0.01-1 MPa, where the catalyst exhibits a fabric, a knitted fabric or a foil as substrate and exhibits a gold/silver mass ratio in the active components applied on the substrate of 0-25, and is obtained by vapor deposition of at least 10% of silver and optionally gold containing active components on the substrate from the gas phase.

公开(公告)号：CO6251304A2

公开(公告)日：2011-02-21

申请号：CO10134474

申请日：2010-10-29

Applicant: BASF SE

Inventor： BOHLING RALF ,  DECKERS ANDREAS ,  KOTREL STEFAN ,  GRITSCH ACHIM

IPC: C01C3/02

Abstract: Proceso para preparar ácido cianhídrico por deshidratación catalítica de formamida gaseosa, donde la deshidratación de la formamida se acopla con una reacción exotérmica por el reactor usado en la deshidratación que comprende dos caminos de fluidos separados los cuales están separados por una pared de reactor común, con una vía fluida que esta proporcionada por la deshidratación de la formamida y la segunda vía fluida que esta proporcionada por la reacción exotérmica. 1.- Un proceso para preparar el ácido cianhídrico por deshidratación catalítica de la formamida gaseosa a una temperatura de 350 a 650°C en un reactor, donde la deshidratación de la formamida esté acoplada con una reacción exotérmica por el reactor que comprende dos vías fluidas separadas que estén separadas por una pared de reactor común, con una vía fluida que este proporcionada por la deshidratación de la formamida y la segunda vía fluida este proporcionada por la reacción exotérmica y la pared del reactor común este hecha del material que tiene una conductividad normal especifica ? de al menos 10 W/mk). 2.- El proceso de acuerdo con la solicitud 1, donde la reacción exotérmica es una combustión catalítica de gas combustible con introducción de oxigeno. 3.- El proceso de acuerdo con la solicitud 2, donde el lado de la pared del reactor común que esté en contacto con el gas combustible tenga una cubierta activa catalíticamente. 4.- El proceso de acuerdo con la solicitud 2 o 3, donde la cubierta esté seleccionada del grupo que consta de metales nobles de los grupos 8B y 1B, aleaciones que comprenden metales de los grupos 8B y/o 1B, óxidos seleccionados de entre MgO, CoO, MoO3, NiO, ZnO, Cr2O3, WO3, SnO, CuO/Cu2O, MnO2 y V2O5, óxidos mezclados seleccionados de CuO-ZnO-Al2O3, CoO-MgO, CoO-La2O3, La2CuO4, Nd2CuO4 y Co-ZnONiO-MoO3, perovskitos seleccionados de entre LaMnO3, CoTiO3, LaTiO3, y CoNiO3 y espineles seleccionados de entre CuAI2O4, MgAI2O4, (Cu, Zn)Al2O4, (Cu, Zn, Ba)Al2O4, (Cu, Zn, Mg)Al2O2, (Cu, Zn, Va)Al2O4 y LaNiO4.

公开(公告)号：EP2885245A4

公开(公告)日：2016-03-30

申请号：EP13879508

申请日：2013-08-13

Applicant: BASF SE

Inventor： HANNEMANN STEFAN ,  GROSSSCHMIDT DIRK ,  ARNOLD MIRKO ,  GRUBERT GERD ,  GERLACH OLGA ,  SUNDERMANN ANDREAS ,  KOTREL STEFAN

IPC: C01B13/34 ,  C01G25/02

CPC classification number: C01B13/34 ,  C01G25/02

公开(公告)号：EP2948653A4

公开(公告)日：2016-08-24

申请号：EP14742867

申请日：2014-01-24

Applicant: BASF CORP ,  BASF SE

Inventor： ARNOLD MIRKO ,  KOTREL STEFAN ,  SIANI ATTILIO ,  SEIMUND STEFAN ,  SCHMITZ THOMAS ,  RABE BURKHARD ,  GRAMICCIONI GARY A ,  SEEL OLIVER ,  NEUBAUER TORSTEN ,  WASSERMANN KNUT

IPC: F01N3/10 ,  B01J23/44 ,  B01J23/46 ,  F01N3/20

CPC classification number: B01J23/63 ,  B01D53/945 ,  B01D2255/1021 ,  B01D2255/1023 ,  B01D2255/1025 ,  B01D2255/407 ,  B01D2255/9022 ,  B01D2255/908 ,  B01D2258/014 ,  B01J35/0006 ,  B01J35/1014 ,  B01J35/1019 ,  B01J35/1061 ,  B01J37/0244 ,  B01J37/0248 ,  F01N3/101 ,  F01N2510/0684 ,  Y02A50/2324 ,  Y02T10/22

Abstract: Provided are catalyst composites whose catalytic material is effective to substantially simultaneously oxidize carbon monoxide and hydrocarbons and reduce nitrogen oxides. The catalyst composites have a two-metal layer on a carrier, the two-metal layer comprising a rhodium component supported by a first support comprising a refractory metal oxide component or a first ceria-zirconia composite; a palladium component supported by a second support comprising a second ceria-zirconia composite; one or more of a promoter, stabilizer, or binder; wherein the amount of the total of the first and second ceria-zirconia composites in the two-metal layer is equal to or greater than the amount of the refractory metal oxide component. Methods of making and using the same are also provided.

公开(公告)号：BR112015017202B1

公开(公告)日：2022-05-17

申请号：BR112015017202

申请日：2014-01-24

Applicant: BASF CORP ,  BASF SE

Inventor： SIANI ATTILIO ,  RABE BURKHARD ,  GARY A GRAMICCIONI ,  WASSERMANN KNUT ,  ARNOLD MIRKO ,  SEEL OLIVER ,  KOTREL STEFAN ,  SEIMUND STEFAN ,  SCHMITZ THOMAS ,  NEUBAUER TORSTEN

IPC: B01J23/44 ,  B01J23/46 ,  F01N3/10 ,  F01N3/20

Abstract: compostos catalisadores automotivos com uma camada de dois metais. são fornecidos compostos catalisadores, cujo material catalítico é eficaz para substancialmente simultaneamente oxidar o monóxido de carbono e hidrocarbonetos e reduzir os óxidos de nitrogênio. os compostos catalisadores têm uma camada de dois metais em um transportador, a camada de dois metais compreendendo um componente de ródio suportado por um primeiro suporte que compreende um componente de óxido metálico refratário ou um primeiro composto de céria-zircônia; um componente de paládio suportado por um segundo suporte que compreende um segundo composto de céria-zircônia; um ou mais de um promotor, estabilizador ou ligante; em que a quantidade total do primeiro e do segundo compostos de céria-zircônia na camada de dois metais é igual ou maior do que a quantidade do componente de óxido metálico refratário. métodos para produzir e usar o mesmo também são fornecidos.

公开(公告)号：ZA201506073B

公开(公告)日：2017-11-29

申请号：ZA201506073

申请日：2015-08-21

Applicant: BASF CORP ,  BASF SE

Inventor： WASSERMANN KNUT ,  GRAMICCIONI GARY A ,  ARNOLD MIRKO ,  NEUBAUER TORSTEN ,  SEEL OLIVER ,  RABE BURKHARD ,  SCHMITZ THOMAS ,  SEIMUND STEFAN ,  SIANI ATTILIO ,  KOTREL STEFAN

Abstract: Provided are catalyst composites whose catalytic material is effective to substantially simultaneously oxidize carbon monoxide and hydrocarbons and reduce nitrogen oxides. The catalyst composites have a two-metal layer on a carrier, the two-metal layer comprising a rhodium component supported by a first support comprising a refractory metal oxide component or a first ceria-zirconia composite; a palladium component supported by a second support comprising a second ceria-zirconia composite; one or more of a promoter, stabilizer, or binder; wherein the amount of the total of the first and second ceria-zirconia composites in the two-metal layer is equal to or greater than the amount of the refractory metal oxide component. Methods of making and using the same are also provided.