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公开(公告)号:DE4132663C2
公开(公告)日:1993-10-14
申请号:DE4132663
申请日:1991-10-01
Applicant: DEGUSSA
Inventor: ARNTZ DIETRICH DR , HAAS THOMAS DR , SCHAEFER-SINDLINGER ADOLF DR
IPC: B01J23/42 , C07B61/00 , C07C29/141 , C07C31/20
Abstract: Process for the preparation of 1,3-propanediol by hydrogenation of hydroxypropionaldehyde (HPA) in aqueous solution on a shaped supported catalyst in a solid bed, the concentration of the HPA in the solution being 5 to 100% by weight, and the hydrogenation being carried out at temperatures from 30 to 180 DEG C and hydrogen pressures from 5 to 300 bar and at a pH between 2.5 and 6.5, characterised in that the supported catalyst consists of titanium oxide, on which platinum is present in finely divided form in an amount relative to the support of 0.1 to 5.0% by weight.
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公开(公告)号:DE4138982A1
公开(公告)日:1993-06-03
申请号:DE4138982
申请日:1991-11-27
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , ARNTZ DIETRICH DR , BRAND REINHOLD DR
Abstract: A process for the production of 3-hydroxyalkanals, more particularly 3-hydroxypropionaldehyde, by hydration of the basic 2-alkenals, more particularly acrolein, in the presence of a solid catalyst containing acid functional groups. The catalysts are based on an inorganic support containing basic activity centers (which are at least partly occupied by a polybasic acid, of which the first pKs value is between 0 and 3, in a form in which it cannot be removed by water) enables the hydration to be carried out with high selectivity. At the same time, the disadvantages of known organic fixed-bed catalysts are avoided. Preferred catalyst are based on pyrogenic titanium dioxide with phosphoric acid fixed thereon.
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公开(公告)号:DE102010030991A1
公开(公告)日:2012-01-12
申请号:DE102010030991
申请日:2010-07-06
Applicant: EVONIK DEGUSSA GMBH
Inventor: HAAS THOMAS DR , TACKE THOMAS DR , PFEFFER JAN CHRISTOPH , KLASOVSKY FLORIAN DR , RIMBACH MICHAEL , VOLLAND MICHAEL , ORTELT MARTINA DR
IPC: C07D307/46 , B01J27/24 , C07D307/48
Abstract: Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung Verbindungen der allgemeinen Formel (I)aus Verbindungen der allgemeinen Formel (IIa) und/oder (IIb).mit einem sauerstoffhaltigen Gas in Gegenwart einer Katalysatorzusammensetzung, wobei die Umsetzung ohne Zusatz von Halogenquellen erfolgt.
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公开(公告)号:DE50115570D1
公开(公告)日:2010-09-09
申请号:DE50115570
申请日:2001-01-08
Applicant: EVONIK DEGUSSA GMBH , UHDE GMBH
Inventor: THIELE GEORG DR , SAUER JOERG DR , HOFEN WILLI , HAAS THOMAS DR
IPC: C07D301/12 , C07D311/12
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公开(公告)号:MY140875A
公开(公告)日:2010-01-29
申请号:MYPI20033683
申请日:2003-09-26
Applicant: EVONIK DEGUSSA GMBH
Inventor: HAAS THOMAS DR , BRASSE CLAUDIA DR , STOCHNIOL GUIDO DR , GLENNEBERG J XDCRGEN DR , LL WOLFGANG W XD
IPC: B01J29/04 , B01J29/89 , C01B15/013 , C01B15/023 , C01B15/037 , C07D301/12 , C07D303/04
Abstract: THE PRESENT INVENTION REFERS TO AN AQUEOUS HYDROGEN PEROXIDE SOLUTION COMPRISING: i) LESS THAN 50 WPPM ALKALI METALS, ALKALINE EARTH METALS ORCOMBINATIONS THEREOF IN TOTAL, IRRESPECTIVE WHETHER THE ALKALI OR ALKALINE EARTH METALS ARE PRESENT IN CATIONIC OR COMPLEX FORM; ii) LESS THAN 50 WPPM OF AMINES HAVING A PK B OF LESS THAN 4.5 OR THE CORRESPONDING PROTONATED COMPOUNDS IN TOTAL; AND iii) AT LEAST 100 WPPM ANIONS OR COMPOUNDS THAT CAN DISSOCIATE TO FORM ANIONS IN TOTAL, WHEREBY THE WPPM ARE BASED ON THE WEIGHT OF HYDROGEN PEROXIDE AND THE CONCENTRATION OF HYDROGEN PEROXIDE IS MORE THAN 50BY WEIGHT BASED ON THE TOTAL WEIGHT OF THE HYDROGEN PEROXIDE SOLUTION,@A PROCESS FOR PREPARATION OF SAID HYDROGEN PEROXIDE SOLUTION AND THE USE OF SAID SOLUTION IN A PROCESS FOR EPOXIDATION OF OLEFINS.
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公开(公告)号:ES2240197T3
公开(公告)日:2005-10-16
申请号:ES00975919
申请日:2000-10-26
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , GLENNEBERG JURGEN , WAGNER RUDOLF , CREUTZ MATTHIAS , SAUER JORG , VANHEERTUM RUDOLF
IPC: B01J8/02 , B01J10/00 , B01J23/44 , B01J35/02 , C01B15/023
Abstract: Procedimiento para la producción de peróxido de hidrógeno según el proceso de la antraquinona, que abarca una etapa de hidrogenación y una etapa de oxidación, en el que en la etapa de hidrogenación una solución de trabajo que contiene una antraquinona-soporte de reacción, y una fase gaseosa que contiene hidrógeno, se conducen a una temperatura de 10 a 100ºC y una presión de 0, 1 a 2 MPa, sobre un lecho fijo consistente en catalizador en forma de partículas dispuesto en un reactor de hidrogenación de forma de columna orientado verticalmente, caracterizado porque el reactor de hidrogenación se hace funcionar como columna de burbujeo, en que una mezcla de la solución de trabajo y fase gaseosa que contiene hidrógeno, se hace pasar con una velocidad de tubo vacío, de la solución de trabajo, de 8 a 100 m/h, de abajo hacia arriba.
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公开(公告)号:DE50010007D1
公开(公告)日:2005-05-12
申请号:DE50010007
申请日:2000-10-26
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , GLENNEBERG JUERGEN , WAGNER RUDOLF , CREUTZ MATTHIAS , SAUER JOERG , VANHEERTUM RUDOLF
IPC: B01J8/02 , B01J10/00 , B01J23/44 , B01J35/02 , C01B15/023
Abstract: In carrying out the hydrogenation stage of the anthraquinone process for the preparation of hydrogen peroxide in a hydrogenation reactor on a fixed bed catalyst of a particulate catalyst, the service life of the catalyst is increased in that the working solution comprising the reaction carrier and a gas phase comprising hydrogen, are passed through the hydrogenation reactor from the bottom upwards. The empty tube speed of the working solution is 0.05 to 100 m/h, preferably 10 to 50 m/h.
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公开(公告)号:DE59806924D1
公开(公告)日:2003-02-20
申请号:DE59806924
申请日:1998-10-20
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , WEBER KARL-LUDWIG DR , STADTMUELLER KLAUS , HOFEN WILLI , VANHEERTUM DR
IPC: B01J23/75 , C07B61/00 , C07C209/48 , C07C209/52 , C07C211/36
Abstract: A process for the production of primary and/or secondary amines from imines or nitriles, comprising an aminating hydrogenation of imine or of nitrile with hydrogen in the presence of ammonia, of a hydrogenation catalyst based on cobalt, nickel, ruthenium or mixtures of these metals and of a base, at a temperature within the range of 50 DEG C. to 200 DEG C. and at a pressure within the range of 0.3 to 30 MPa. The yield of amine is increased by the use of a quaternary ammonium hydroxide as base. Preferably a tetraalkylammonium hydroxide is used in a quantity of from 0.01 to 100 mMol per mol of amine or of nitrile. The process is suitable in particular for the production of isophoronediamine from isophorone nitrile imine.
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公开(公告)号:BR9904064A
公开(公告)日:2000-09-19
申请号:BR9904064
申请日:1999-09-02
Applicant: DEGUSSA
Inventor: MORAWIETZ MARCUS DR , HAAS THOMAS DR , BURKHAARDT OLAF DR , WANHEERTUM RUDOLF DR
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公开(公告)号:BR9804476A
公开(公告)日:1999-12-07
申请号:BR9804476
申请日:1998-11-06
Applicant: DEGUSSA
Inventor: MORAWIETZ MARCUS DR , HAAS THOMAS DR , BURKHARDT OLAF DR , VANHEERTUM RUDOLF DR
IPC: B01J29/72 , B01J31/04 , C07B61/00 , C07C29/10 , C07C31/12 , C07C31/18 , C07C31/20 , C07C31/24 , C07C41/09 , C07C43/13 , C07C43/10
Abstract: Intermolecular etherification of mono- or multivalent alcohols is carried out in the presence of an additional acid-stable hydrogenation catalyst in a hydrogen atmosphere. Process for the intermolecular etherification of mono- or multivalent alcohols and ether splitting comprises treating the alcohol in the case of etherification or the ether in the case of ether splitting in the aqueous phase in the presence of an acid catalyst at at least 100 degrees C and then treatment is carried out using an acid-stable hydrogenation catalyst in a hydrogen atmosphere.
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