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公开(公告)号:JP2002012408A
公开(公告)日:2002-01-15
申请号:JP2001147601
申请日:2001-05-17
Applicant: DMC2 DEGUSSA METALS CATALYSTS CERDEC AG
Inventor: WIELAND STEFAN DR , BAUMANN FRANK , AHLBORN RAINER
Abstract: PROBLEM TO BE SOLVED: To provide a method of autothermal catalytic reforming for a hydrocarbon to introduce an initial mixture of the hydrocarbon heated up to preheating temperature with oxygen and water or steam on a catalyst. SOLUTION: The method is characterized by being thermally insulated and having the catalyst covered with aluminum oxide, silicon dioxide, titanium dioxide, or the mixture of these oxides on a carrier and with a catalytic material which contains at least a kind of platinum group metal on a zeolite group oxide carrier.
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公开(公告)号:JPH1043597A
公开(公告)日:1998-02-17
申请号:JP7692697
申请日:1997-03-28
Applicant: DEGUSSA
Inventor: LANSINK-ROTGERINK HERMANUS G J , HOECKER HARALD DR , WIELAND STEFAN DR , SEEBALD STEFFEN DR , RIEDEMANN HEIKE
Abstract: PROBLEM TO BE SOLVED: To improve the aging stability of a phosphoric acid catalyst under hydrothermal conditions by incorporating a specified amt. of TiO2 or ZrO2 into the carrier of the catalyst contg. a specified amt. of H3 PO4 . SOLUTION: This phosphoric acid catalyst contains H3 PO4 as an active component by 1-50wt.% of the total amt. on the molded inorg. carrier contg. TiO2 or ZrO2 by at least 90wt.% of the total amt. of the pure carrier. The sizes of the constituent molded bodies of this catalyst are in the range of about 1-10mm and molded bodies each having about 2-5mm size are advantageously used. This catalyst is used for hydration of olefin, e.g. hydration of ethylene for producing ethanol and diethyl ether and hydration of propylene for producing isopropanol.
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公开(公告)号:JP2001322803A
公开(公告)日:2001-11-20
申请号:JP2001081397
申请日:2001-03-21
Applicant: DMC2 DEGUSSA METALS CATALYSTS CERDEC AG
Inventor: BAUMANN FRANK , WIELAND STEFAN DR
IPC: C01B3/48 , B01J23/38 , B01J23/56 , B01J23/89 , C01B3/16 , C01B3/58 , C10K3/04 , H01M8/04 , H01M8/06
Abstract: PROBLEM TO BE SOLVED: To provide a method of converting carbon monoxide in a gaseous mixture containing hydrogen and another oxidizable components into carbon dioxide and hydrogen by catalytically reacting with water. SOLUTION: A shift catalyst is a noble metal based oxidation active one and the operation temperature necessary for the catalyst is controlled and if necessary kept by the partial oxidation of the oxidizable components in the gaseous mixture.
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公开(公告)号:JPH10218817A
公开(公告)日:1998-08-18
申请号:JP2077698
申请日:1998-02-02
Applicant: DEGUSSA
Inventor: WIELAND STEFAN DR , GRADL ROBERT , ROEDER STEFAN
IPC: B01J31/02 , C07B61/00 , C07C37/20 , C07C39/16 , C07C39/367
Abstract: PROBLEM TO BE SOLVED: To produce 2,2'-bis(4-hydroxyphenyl)propane in high yield by adding water to the reaction mixture and reacting phenol with a carbonyl compound in the presence of an organopolysiloxane containing sulfonate group and mercapto group or an inorganic carrier material modified by the sulfonate group and the mercapto group. SOLUTION: A compound of formula I (R to R are each H, a 1-4C alkyl, etc.), (e.g. phenol) is reacted with a compound of formula II (R and R are each H, a 1-6C alkyl, etc.), (e.g. formaldehyde) in the presence of an organopolysiloxane containing sulfonate group and mercapto group by allowing the reaction mixture to include 0.1-30wt.% water, preferably at 50-70 deg.C to provide the objective compound of formula III. This method is useful for producing highly pure bisphenol A having high isomer ratio of a p, p-product/an o, p- product.
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公开(公告)号:JPH1087572A
公开(公告)日:1998-04-07
申请号:JP17826397
申请日:1997-07-03
Applicant: DEGUSSA
Inventor: HAAS THOMAS DR , ARNTZ DIETRICH DR , WEBER KARL-LUDWIG DR , HOFEN WILLI , WIELAND STEFAN DR
IPC: C07C209/24 , C07B61/00 , C07C209/26 , C07C209/48 , C07C209/52 , C07C211/01 , C07C211/33 , C07C211/36 , C07C211/43
Abstract: PROBLEM TO BE SOLVED: To provide a method for production a primary and/or secondary amine from an oxo compound suppressing the formation of byproduct by using an organopolysiloxane containing a sulfonate group as a catalyst for turning the oxo compound into imino and turning the oxo compound into an imino with excess ammonia. SOLUTION: An oxo compound is turned into an imino with excess ammonia in a case of a primary amine or with a lower monoalkylamine in a case of a secondary amine respectively by using an organopolyusiloxane containing a sulfonate group as a catalyst, if necessary, in the presence of an organic solvent, and hydrogenating the resultant reaction product in the presence of a hydrogenation catalyst at 20-250 deg.C under 0.5-25MPa pressure to provide the objective amine in the method for producing the primary and/or secondary amine from the oxo compound.
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公开(公告)号:JP2002153737A
公开(公告)日:2002-05-28
申请号:JP2001245737
申请日:2001-08-13
Applicant: DMC2 DEGUSSA METALS CATALYSTS CERDEC AG
Inventor: KEMPF BERND , KUHN WERNER , DROST ERNST , BEYER HANS HERMANN , ROOS MEIKE , WIELAND STEFAN DR
IPC: B01D69/10 , B01D53/22 , B01D67/00 , B01D71/02 , B23K20/00 , B23K20/04 , B23K20/08 , C01B3/50 , C22C5/04 , C22C5/06 , C22F1/00 , C22F1/14 , H01M8/0662
Abstract: PROBLEM TO BE SOLVED: To provide a method of manufacturing a metallic composite film, of which the metallic film and film support consist of two different metals or metal alloys and which contains a thin metallic film of a desired thickness and a metal film support having a porous structure. SOLUTION: A precursor of the metallic film is set on a nonporous precursor of the metal support, and a metal composite material is made between both precursors. The desired thickness of the metallic film is adjusted by the deformation of the metal composite material, subsequently the porous structure of the film support is produced.
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公开(公告)号:JP2002126474A
公开(公告)日:2002-05-08
申请号:JP2001245739
申请日:2001-08-13
Applicant: DMC2 DEGUSSA METALS CATALYSTS CERDEC AG
Inventor: DROST ERNST , KUHN WERNER , ROOS MEIKE , WIELAND STEFAN DR , KEMPF BERND
IPC: B01D69/10 , B01D53/22 , B01D67/00 , B01D71/02 , C01B3/50 , C23C14/34 , C23C16/06 , C23C28/00 , H01M4/94 , H01M8/0662 , H01M8/04
Abstract: PROBLEM TO BE SOLVED: To provide a supported metal membrane for separating hydrogen from a gaseous mixture, in which a membrane-supporting body has a high porosity which has hitherto never been realized. SOLUTION: A metal membrane is arranged on the supporting surface of the membrane-supporting body. At this time, pores of the membrane-supporting body are each filled with an auxiliary material at least in the range of the surface of the supporting body before arranging the metal membrane, and each hole is opened by removing the auxiliary material after arranging the metal membrane.
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公开(公告)号:JP2001316682A
公开(公告)日:2001-11-16
申请号:JP2001079295
申请日:2001-03-19
Applicant: DMC2 DEGUSSA METALS CATALYSTS CERDEC AG
Inventor: BAUMANN FRANK , WIELAND STEFAN DR
Abstract: PROBLEM TO BE SOLVED: To provide a process for the conversion of carbon monoxide in a hydrogen-containing gas mixture which has a high specific conversion ratio of carbon monoxide with a good selectivity under the moving use condition of automobiles that an output requirement changes rapidly, has a high temperature-stability, and has no sensitivity to the oxygen in the educt gas mixture. SOLUTION: The subject process comprises a catalytic conversion of carbon monoxide is catalytically converted into carbon dioxide and water by means of the water in a hydrogen-containing gas mixture by passing through the gas mixture over a shift catalyst at an operating temperature for the purpose of the conversion of carbon monoxide. In this case, the shift catalyst is at least one noble metal applied on an inactive support element in the shape of a covered material.
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公开(公告)号:JP2000354764A
公开(公告)日:2000-12-26
申请号:JP2000148695
申请日:2000-05-19
Applicant: DEGUSSA
Inventor: WIELAND STEFAN DR , BAUMANN FRANK , ADAM FRANK , ANDERSCH STEFAN
IPC: B01J21/12 , B01J23/60 , B01J23/80 , B01J29/068 , B01J35/10 , B01J37/00 , B01J37/02 , B01J37/14 , B01J37/16 , B01J37/18 , C01B3/32 , H01M8/06
Abstract: PROBLEM TO BE SOLVED: To obtain a high selectivity and a specific hydrogen productivity in a reforming reaction of alcohol with steam by depositing a catalytically active component on at least one kind of carrying material selected from a group consisting of aluminum oxide, aluminum silicate, titanium oxide, zirconium oxide, zeolite, and mixtures thereof or a mixed oxide. SOLUTION: A catalytically active component is deposited on at least one kind of carrying material selected from a group consisting of aluminum oxide, aluminum silicate, titanium oxide, zirconium oxide, zeolite and mixtures thereof or a mixed oxide. This catalyst contains a 0.5-10 mass % palladium/zinc alloy and 1-50 mass % zinc oxide to the total mass of the catalyst respectively. When methanol is reformed with steam, this catalyst can provide >20 Nm3/kg.h hydrogen producing capacity at 300 deg.C reactor temperature. And the carrying material used is aluminum oxide having >10 m2/g BET specific surface area.
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公开(公告)号:JPH10182668A
公开(公告)日:1998-07-07
申请号:JP34508197
申请日:1997-12-15
Applicant: DEGUSSA
Inventor: BALDUF TORSTEN DR , WIELAND STEFAN DR , LORTZ WOLFGANG DR , POHLISCH JOACHIM DR , GOEBEL THOMAS DR , GRETHE HORST
IPC: C07F7/18
Abstract: PROBLEM TO BE SOLVED: To provide a continuous production process for γ-aminopropyl- trialkoxysilane. SOLUTION: (A) γ-Chloropropyltrialkoxysilane and ammonia are mixed at a desired ratio, (B) the mixture is heated up to the reaction temperature, (C) allowed to recycle in the pressurized reactor for the residence time for the complete reaction. At this time, the reaction mixture may be circulated through a plurality of temperature zones. Then, (D) the reaction mixture is cooled down, when necessary, an organic solvent (an extractant) is added, (E) the product is separated from the two-phase mixture and (F) the ammonia phase is returned to the reactor (C) or to (A).
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