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公开(公告)号:DE19749201A1
公开(公告)日:1999-08-12
申请号:DE19749201
申请日:1997-11-07
Applicant: DEGUSSA
Inventor: MORAWIETZ MARCUS DR , HAAS THOMAS DR , BURKHARDT OLAF DR , VANHEERTUM RUDOLF DR
IPC: B01J31/04 , C07B61/00 , C07C29/10 , C07C31/12 , C07C31/18 , C07C31/20 , C07C31/24 , C07C41/09 , C07C43/13 , B01J29/72 , C07C43/04
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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公开(公告)号:DE19747913C1
公开(公告)日:1999-02-11
申请号:DE19747913
申请日:1997-10-30
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , WEBER KARL-LUDWIG DR , STADTMUELLER KLAUS , HOFEN WILLI , VANHEERTUM RUDOLF 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, preferably for the production of 3 monomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine) from 3- cyano-3,5,5-trimethylcyclohexane-imine (isophoronenitrile-imine) is claimed. The imine or nitrile is subjected to an amination-hydrogenation process using hydrogen in the presence of ammonia, a cobalt, nickel and/or ruthenium based hydrogenation catalyst and a hydroxide base at 50-250 deg C and 0.3-30 MPa and work up of a the reaction mixture. The amination-hydorgenation process is carried out in the presence of a quat. ammonium hydroxide.
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公开(公告)号:DE59303861D1
公开(公告)日:1996-10-24
申请号:DE59303861
申请日:1993-10-18
Applicant: DEGUSSA
Inventor: NEHER ARMIN DR , HAAS THOMAS DR , ARNTZ DIETRICH DR , KLENK HERBERT DR , GIRKE WALTER
Abstract: A process for the production of acrolein by dehydration of glycerol in the liquid phase or in the gaseous phase, in each case on acidic solid catalysts, is described. Compared with previously known processes, the space-time yield and catalyst service life may be surprisingly increased with higher selectivity by treating a glycerol-water mixture with a glycerol content of 10 to 40 wt. % at 180 DEG to 340 DEG C. (liquid phase) or at 250 DEG to 340 DEG C. (gaseous phase) on a solid catalyst with an Ho value (Hammett acidity function) of less than +2, preferably less than -3.
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公开(公告)号:DK0544118T3
公开(公告)日:1995-09-25
申请号:DK92118470
申请日:1992-10-29
Applicant: DEGUSSA
Inventor: ARNTZ DIETRICH DR , HAAS THOMAS DR , BOEHME GEORG
Abstract: The invention relates to a process for the preparation of 3-hydroxyalkanals having 3 to 12, in particular 3 or 4, C atoms, by hydration of the basic 2-alkenals with water in a homogeneous phase in the presence of an acidic catalyst. The previously known hydration by means of mineral acids or carboxylic acids as catalyst results in poor space-time yields and/or poor selectivities. These disadvantages can be avoided when a dissolved acid/base buffer is used as catalyst which results in a pH of 2 to 5 in the reaction mixture and whose acid component and the corresponding base are present in the reaction mixture in an amount of 0.5 to 40% by weight in total. The preferred buffers composed of a lower monobasic carboxylic acid and a tertiary amine can be recycled in a simple manner.
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公开(公告)号:DE4343890A1
公开(公告)日:1995-06-29
申请号:DE4343890
申请日:1993-12-22
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , ARNTZ DIETRICH DR , MOST DIETER DR
IPC: B01J23/44 , B01J8/02 , B01J8/04 , B01J23/46 , B01J23/75 , C07B61/00 , C07C209/26 , C07C209/48 , C07C211/36 , C07C211/35 , C07C255/46
Abstract: The invention is aimed at an improved process for the continuous preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine in high yield and high purity (isophoronediamine) from 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile) by aminating hydrogenation with hydrogen and ammonia in the presence of a solid bed catalyst. Isophoronediamine is a raw material for the preparation of isophoronediisocyanate, an amine component for polyamides and a curing component for epoxy resins. According to the invention, the aminating hydrogenation is carried out by allowing a mixture of isophoronenitrile, ammonia and a C1-C3-alcohol to trickle over a trickle-bed reactor provided with a Co and/or Ru solid-bed catalyst at 3 to 8 MPa and a temperature of 40 to 150 DEG C, preferably 90 to 130 DEG C, in the presence of hydrogen and working up the reaction mixture by distillation. A high-boiling by-product fraction, containing a bicyclic amidine, is preferably added to the mixture to be hydrogenated, whereby the yield is appreciably increased.
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公开(公告)号:DE102010015807A1
公开(公告)日:2011-10-20
申请号:DE102010015807
申请日:2010-04-20
Applicant: EVONIK DEGUSSA GMBH
Inventor: POETTER MARKUS DR , SCHMID ANDREAS DR , BUEHLER BRUNO DR , HENNEMANN HANS-GEORG DR , JULSING MATTIJS KAMIEL , SCHAFFER STEFFEN DR , HAAS THOMAS DR , SCHREWE MANFRED , CORNELISSEN SJEF , ROOS MARTIN DR , HAEGER HARALD DR
Abstract: Gegenstand der Erfindung ist ein biokatalytisches verfahren zur Oxidation von organischen Verbindungen unter Zuhilfenahme eines alkL-Genproduktes sowie in diesem Verfahren eingesetzte Mikroorganismen.
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公开(公告)号:DE102009054984A1
公开(公告)日:2011-06-22
申请号:DE102009054984
申请日:2009-12-18
Applicant: EVONIK DEGUSSA GMBH
Inventor: SCHUBERT ANJA , HAAS THOMAS DR , SCHAFFER STEFFEN DR , TACKE THOMAS DR
Abstract: Gegenstand der Erfindung ist ein Verfahren zur Isolierung von Stilbenoiden aus Lösungsmitteln sowie die Verwendung der hiermit erhaltenen Stilbenoide.
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公开(公告)号:MY136051A
公开(公告)日:2008-08-29
申请号:MYPI20034450
申请日:2003-11-20
Applicant: EVONIK DEGUSSA GMBH , UHDE GMBH
Inventor: HAAS THOMAS DR , BRASSE CLAUDIA DR , HOFEN WILLI , STOCHNIOL GUIDO DR , WOELL WOLFGANG
IPC: C07D301/12
Abstract: THE PRESENT INVENTION REFERS TO A PROCESS FOR THE CATALYST EPOXIDATION OF OLEFINS IN THE PRESENCE OF A TITANIUM CONTAINING ZEOLITE CATALYST AND A POLAR SOLVENT WHEREBY THE DEACTIVATION OF THE CATALYST UPON RECYCLING OF THE SOLVENT HAS BEEN CONSIDERABLY REDUCED. IN THE PROCESS ONE OR MORE NITROGEN CONTAINING COMPOUNDS ARE INTRODUCED AT SOME STAGE, A SOLVENT STREAM IS RECOVERED, TREATED TO CONTAIN LESS THAN 50WPPM NITROGEN IN THE FORM OF ORGANIC NITROGEN COMPOUNDS AND AT LEAST A PART OF IT IS RECYCLED TO THE EPOXIDATION STEP. THE INVENTION IS ALSO DIRECTED TOWARDS' A PROCESS FOR THE CATALYTIC EPOXIDATION OF PROPENE WHICH INTEGRATES THE INVENTIVE TREATMENT AND RECYCLE OF THE SOLVENT INTO THE WORKUP OF THE REACTION MIXTURE.
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公开(公告)号:AT231118T
公开(公告)日:2003-02-15
申请号:AT98119852
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:DE19721897A1
公开(公告)日:1998-12-03
申请号:DE19721897
申请日:1997-05-26
Applicant: DEGUSSA
Inventor: SAUER JOERG DR , HAAS THOMAS DR , KELLER BRUNO DR , FREUND ANDREAS DR , BURKHARDT WERNER , MICHELCHEN DIETRICH , BERWEILER MONIKA
IPC: B01J25/00 , B01J37/00 , C07B31/00 , C07B61/00 , C07C209/48 , B01J25/02 , C07B35/04 , C07B35/02 , C07B33/00 , C07C27/02
Abstract: A formed metal solid-bed catalyst, consisting entirely of catalyst alloy (and possibly promoters) with a total pore vol. of 0.1-0.6 ml/g and with a surface shell 0.1-2.0 mm thick which is activated by complete or partial leaching of an extractable alloy component (I). Also claimed is a process for the production of thE catalyst . Preferably the catalyst metal is nickel, cobalt, copper and/or iron, and component (I) is aluminium, zinc or silicon. The catalyst may also contain up to 15 wt% chromium, iron, cobalt, tantalum, molybdenum and/or titanium as promoters.
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