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公开(公告)号:DE102011100772A1
公开(公告)日:2012-11-08
申请号:DE102011100772
申请日:2011-05-05
Applicant: EVONIK DEGUSSA GMBH
Inventor: ZEHNACKER OLIVIER , GRAMMANN KATRIN DR , HOLTKAMP MANUEL , WOLTER JAN , HUELLER THOMAS , MOHR ALEXANDER , GRIMBERG GERLIND , HAAS THOMAS DR , HABERLAND JUERGEN DR
Abstract: Gegenstand der vorliegenden Erfindung ist ein Verfahren zur Herstellung von Isomaltulose umfassend die Verfahrensschritte A) in Kontakt Bringen eines immobilisierten Enzymkomplexes, welches die Umsetzung von Saccharose zu Isomaltulose zu katalysieren vermag, mit einer saccharosehaltigen Lösung; B) Isomerisierung mindestens eines Teiles der Saccharose zu Isomaltulose; C) Abtrennen des Enzymkomplexes und gegebenenfalls D) weiteres Aufreinigen der Isomaltulose, dadurch gekennzeichnet, dass als saccharosehaltige Lösung mindestens einer ausgewählt aus Dicksaft oder Dünnsaft, bevorzugt Dicksaft, eingesetzt wird.
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公开(公告)号:ES2322033T3
公开(公告)日:2009-06-16
申请号:ES02012040
申请日:2002-05-31
Applicant: EVONIK DEGUSSA GMBH
Inventor: STOCHNIOL GUIDO DR , JAGER BERND DR , HAAS THOMAS DR , FINKE NORBERT DR , BURKHARDT WERNER , GRUNERT JURGEN
IPC: B01J23/46 , B01J35/10 , C07B61/00 , C07C209/72 , C07C211/36
Abstract: Procedimiento para la hidrogenación de una amina aromática que presenta al menos un grupo amino unido a un núcleo aromático, que comprende la reacción de la amina aromática con hidrógeno en presencia de un catalizador soportado que como metal activo contiene, aplicado sobre un soporte, rutenio solo o junto con al menos un metal de los subgrupos I, VII u VIII del sistema periódico de los elementos, en una cantidad, respecto al catalizador soportado, de 0,01 a 20% en peso de metales activos, caracterizado porque el soporte del catalizador presenta una superficie BET en el intervalo de más de 30 m 2 /g a menos de 70 m 2 /g y más del 50% del volumen de los poros del soporte del catalizador son macroporos con un diámetro de poro superior a 50 nm y menos del 50% son mesoporos con un diámetro de poro de 2 a 50 nm, y porque el metal activo aplicado sobre el catalizador presenta una profundidad de penetración en el soporte en el intervalo de 20 a 500 µm, en especial de 25 a 250 µm.
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公开(公告)号:MY135540A
公开(公告)日:2008-05-30
申请号:MYPI20031593
申请日:2003-04-28
Applicant: EVONIK DEGUSSA GMBH , UHDE GMBH
Inventor: BERGES JOSE , THIELE GEORG DR , ULLRICH NORBERT , WOELL WOLFGANG , BRASSE CLAUDIA DR , EICKHOFF HUBERTUS , HAAS THOMAS DR , HOFEN WILLI , KAMPEIS PERCY DR , MOROFF GERALD , POHL WERNER , STOCHNIOL GUIDO DR
IPC: C07D301/12 , C07B61/00 , C07D303/04
Abstract: THE PRESENT INVENTION RELATES TO A PROCESS FOR THE EPOXIDATION OF OLEFINS COMPRISING I) REACTING AN OLEFIN WITH HYDROGEN PEROXIDE IN PRESENCE OF AN EPOXIDATION CATALYST AND AN ALCOHOLIC SOLVENT; II) SEPARATING PRODUCT OLEFIN OXIDE AND UNREACTED OLEFIN FROM THE REACTION PRODUCT OF STEP I); III) RECOVERING A STREAM COMPRISING THE ALCOHOLIC SOLVENT; AND IV) SUBJECTING THE RECOVERED STREAM OF STEP III) TO HYDROGENATION.
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公开(公告)号:MY131852A
公开(公告)日:2007-09-28
申请号:MYPI20033684
申请日:2003-09-26
Applicant: EVONIK DEGUSSA GMBH , UHDE GMBH
Inventor: HAAS THOMAS DR , BRASSE CLAUDIA DR , STOCHNIOL GUIDO DR , HOFEN WILLI , WOELL WOLFGANG , THIELE GEORG DR
IPC: C07D301/12
Abstract: THE PRESENT INVENTION REFERS TO A CONTINUOS PROCESS FOR THE EPOXIDATION OF OLEFINS WITH HYDROGEN PEROXIDE IN PRESENCE OF A HETEROGENEOUS CATALYST PROMOTING THE EPOXIDATION REACTION.WHEREBY THE AQUEOUS REACTION MIXTURE COMPRISES: I) AN OLEFIN;II) HYDROGEN PEROXIDE; III) LESS THAN 100 WPPM OF ALKALI METALS. EARTH ALKALI METALS, BOTH IRRESPECTIVE WHETHER IN IONIC, COMPLEX OR COVALENTLY BONDED FORM, BASES OR CATIONS OF BASES HAVING A PKB OF LESS THAN 4.5, OR COMBINATIONS THEREOF; AND IV) AT LEAST 100 WPPM OF BASES OR CATIONS OF BASES HAVING A PKB OF AT LEAST 4.5 OR COMBINATIONS THEREOF,WHEREBY THE WPPM ARE BASED ON THE TOTAL WEIGHT OF HYDROGEN PEROXIDE IN THE REACTION MIXTURE.
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公开(公告)号:AR032928A1
公开(公告)日:2003-12-03
申请号:ARP020100746
申请日:2002-03-01
Applicant: DEGUSSA , KRUPP UHDE GMBH
Inventor: HAAS THOMAS DR , HOFEN WILLI , SAUER JOERG DR , THIELE THOMAS DR
IPC: C07D301/12 , C07D303/04
Abstract: Un proceso para la epoxidacion catalítica de olefinas con peroxido de hidrogeno en un sistema de reaccion de flujo continuo, donde la mezcla de reaccion se hace pasar a través de un lecho fijo de catalizador en el interior de un reactor equipado con dispositivos de enfriamiento mientras se mantiene un perfil térmico dentro del reactor de modo tal que la temperatura del medio de enfriamiento del dispositivo de enfriamiento sea de al menos 40 degree C y la temperatura máxima dentro del lecho de catalizador sea de 60 degree C como máximo.
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公开(公告)号:BR9804474A
公开(公告)日:2000-02-29
申请号:BR9804474
申请日:1998-11-06
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , BURKHARDT OLAF DR , MORAWIETZ MARCUS DR , WANHEERTUM RUDOLF DR , BOURREL AGNES
IPC: C07D307/20 , C07B35/06 , C07C20060101 , C07C41/09 , C07C43/18 , C07D307/06 , C07D307/08 , C07D309/04 , C07D493/04 , C07H1/00 , C07H3/00
Abstract: Process for producing 5- or 6-membered cyclic ethers (anhydropolyols) comprises subjecting polyols having at least 4 C atoms and at least 2 OH groups to cyclodehydration at at least 100 degrees C in the presence of water, an acid catalyst, an acid-stable hydrogenation catalyst and hydrogen. Preferably the reaction temperature is 100-380 degrees C, preferably 180-280 degrees C. The H2 pressure is 1-20 MPa, preferably 3-10 MPa. The hydrogenation catalyst comprises Ru, Rh, Pd and/or Pt as metals or metal compounds. The hydrogenation catalyst is used in an amount of 0.001-10 (preferably 0.01-1) wt.% based on the polyol. The acid catalyst is a 1-10C aliphatic carboxylic acid, preferably formic, acetic or propionic acid. The acid catalyst is used in an amount of 0.1-20 (especially 0.5-10) wt.% based on the polyol. The polyol is a tetritol, pentitol or hexitol.
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公开(公告)号:DE19629372A1
公开(公告)日:1998-01-22
申请号:DE19629372
申请日:1996-07-20
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , MEIER MARTIN DR , BROSMER CHRISTOPH DR , ARNTZ DIETRICH DR , FREUND ANDREAS DR
IPC: C07C51/235 , C07C55/08 , C07C51/21
Abstract: In the preparation of malonic acid (I) or its salts by catalytic oxidation of a starting material (II) with 3 carbon (C) atoms with (gas) containing oxygen (O2) in the presence of a platinum-group noble metal catalyst in aqueous phase at pH \- 6 and isolation of (I) or its salts, (II) is 3-hydroxypropionaldehyde (IIA) or 3-hydroxypropionic acid (IIB) and the amount of catalyst used corresponds to
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公开(公告)号:DE19629371A1
公开(公告)日:1998-01-22
申请号:DE19629371
申请日:1996-07-20
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , BROSMER CHRISTOPH DR , MEIER MARTIN DR , ARNTZ DIETRICH DR , FREUND ANDREAS DR
Abstract: The preparation of 3-hydroxypropionic acid (I) or its salts comprises by catalytic oxidation of 3-hydroxypropionaldehyde (II) with oxygen or oxygen-containing gas in the presence of a platinum-group noble metal M as catalyst in aqueous phase and isolation of (I) or its salts. The amount of M is 10 wt.% with respect to (II).
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公开(公告)号:DK0659733T3
公开(公告)日:1998-01-05
申请号:DK94118077
申请日:1994-11-17
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , ARNTZ DIETRICH DR , MOST DIETER DR
IPC: B01J23/75 , C07B61/00 , B01J23/46 , C07C209/26 , C07C209/48 , C07C211/36
Abstract: 3-Aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine) is a raw material which is used industrially for various synthetic resins. Isophoronediamine is used as a cis/trans isomer mixture, the cis/trans isomer ratio influencing the properties. The invention shows a way of controlling the isomer ratio in the preparation of isophoronediamine by aminating hydrogenation of 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile) in the presence of ammonia, H2 and a catalyst. The reaction is carried out in two temperature stages, namely first at 10 to 90 DEG C and then at 90 to 150 DEG C with a temperature difference between both stages of at least 30 DEG C, the contact time in the first stage being shorter than in the second. By lowering the temperature in the first stage the cis/trans ratio is increased.
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公开(公告)号:AT156801T
公开(公告)日:1997-08-15
申请号:AT94118077
申请日:1994-11-17
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , ARNTZ DIETRICH DR , MOST DIETER DR
IPC: B01J23/46 , B01J23/75 , C07B61/00 , C07C209/26 , C07C209/48 , C07C211/36
Abstract: 3-Aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine) is a raw material which is used industrially for various synthetic resins. Isophoronediamine is used as a cis/trans isomer mixture, the cis/trans isomer ratio influencing the properties. The invention shows a way of controlling the isomer ratio in the preparation of isophoronediamine by aminating hydrogenation of 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile) in the presence of ammonia, H2 and a catalyst. The reaction is carried out in two temperature stages, namely first at 10 to 90 DEG C and then at 90 to 150 DEG C with a temperature difference between both stages of at least 30 DEG C, the contact time in the first stage being shorter than in the second. By lowering the temperature in the first stage the cis/trans ratio is increased.
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