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公开(公告)号:DE10331771A1
公开(公告)日:2005-02-03
申请号:DE10331771
申请日:2003-07-11
Applicant: BASF AG
Inventor: WESSEL HELGE , HOELZLE MARKUS , WILDEN NORBERT , HESSE MICHAEL
IPC: B01D53/86 , C10L3/10 , B01D53/48 , B01J21/04 , B01J23/882
Abstract: Removal of sulfur compounds from gases containing hydrocarbons is carried out using catalysts (I) (other than activated carbon or zeolites) containing one or more of copper, silver, zinc, molybdenum, iron, cobalt and/or nickel, at -50 to +150[deg]C and 0.1-10 bars. An independent claim is included for new catalysts (I'), comprising 1-99.8 wt. % copper, silver, zinc, molybdenum, iron, cobalt and/or nickel and 0.2-99 wt. % oxides of Group IIB, IIIB, IVB, VIB, VIII, IIIA or IVA elements, which are solid at least up to 250[deg]C.
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公开(公告)号:NO20044561L
公开(公告)日:2004-11-26
申请号:NO20044561
申请日:2004-10-22
Applicant: BASF AG
Inventor: HESSE MICHAEL , HARTH KLAUS , HOFSTADT OTTO , SCHINDLER GOTZ-PETER , SIMON FALK
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , C07C5/327
Abstract: The invention relates to a process for preparing a catalyst support, in which zirconium dioxide powder is mixed with a binder, if desired a pore former, if desired an acid, water and, if desired, further additives to give a kneadable composition and the composition is homogenized, shaped to produce shaped bodies, dried and calcined, wherein the binder is a monomeric, oligomeric or polymeric organosilicon compound. Suitable binders are monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halosilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also provides the catalyst support which has been prepared in this way, a catalyst comprising the support and its use as dehydrogenation catalyst.
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公开(公告)号:NO20044561A
公开(公告)日:2004-11-26
申请号:NO20044561
申请日:2004-10-22
Applicant: BASF AG
Inventor: HESSE MICHAEL , HARTH KLAUS , HOFSTADT OTTO , SCHINDLER GOTZ-PETER , SIMON FALK
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , C07C5/327
CPC classification number: C07C5/3332 , B01J21/066 , B01J23/002 , B01J23/63 , B01J35/002 , B01J35/10 , B01J35/109 , B01J37/0009 , B01J37/0018 , B01J2523/00 , C07C2521/06 , Y02P20/52 , C07C11/06 , B01J2523/13 , B01J2523/15 , B01J2523/3706 , B01J2523/41 , B01J2523/43 , B01J2523/48 , B01J2523/828
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公开(公告)号:AT281423T
公开(公告)日:2004-11-15
申请号:AT00960507
申请日:2000-08-22
Applicant: BASF AG
Inventor: HUBER SYLVIA , SPRAGUE MICHAEL JOLYON , BREITSCHEIDEL BORIS , WULFF-DOERING JOACHIM , HESSE MICHAEL , PINKOS ROLF , LIANG SHELUE , KUMBERGER OTTO , WALTER MARC
IPC: B01J23/80 , C07B61/00 , C07C29/149 , C07C31/04 , C07C31/20
Abstract: A process for the hydrogenation of an organic compound containing at least one carbonyl group comprises bringing the organic compound in the presence of hydrogen into contact with a shaped body which can be produced by a process in which (i) an oxidic material comprising copper oxide, zinc oxide and aluminum oxide is made available, (ii) pulverulent metallic copper or pulverulent cement or a mixture thereof is added to the oxidic material, and (iii) the mixture resulting from (ii) is shaped to form a shaped body.
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公开(公告)号:DE50103810D1
公开(公告)日:2004-10-28
申请号:DE50103810
申请日:2001-12-07
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , STEIN FRANK , PINKOS ROLF , HESSE MICHAEL , SPRAGUE JOLYON , ROESCH MARKUS , BORCHERT HOLGER , SCHLITTER STEPHAN , RAHN RALF-THOMAS , WECK ALEXANDER
IPC: B01J23/72 , B01J23/80 , C07C27/06 , C07D307/08
Abstract: Unsubstituted or alkyl-substituted THF is obtained by catalytic hydrogenation in the gas phase of C4-dicarboxylic acids and/or their derivatives using a catalyst comprising 20% by weight, preferably >30% by weight, in particular from 35 to 90% by weight, of an oxidic support having acid centers, at a hot spot temperature of from 240 to 310° C., preferably from 240 to 280° C., and a WHSV over the catalyst of from 0.01 to 1.0, preferably from 0.02 to 1, in particular from 0.05 to 0.5, kg of starting material/l of catalystxhour.
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公开(公告)号:AT276986T
公开(公告)日:2004-10-15
申请号:AT01985854
申请日:2001-12-07
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , STEIN FRANK , PINKOS ROLF , HESSE MICHAEL , SPRAGUE MICHAEL JOLYON , ROESCH MARKUS , BORCHERT HOLGER , SCHLITTER STEPHAN , RAHN RALF-THOMAS , WECK ALEXANDER
IPC: B01J23/72 , B01J23/80 , C07C27/06 , C07D307/08
Abstract: Unsubstituted or alkyl-substituted THF is obtained by catalytic hydrogenation in the gas phase of C4-dicarboxylic acids and/or their derivatives using a catalyst comprising 20% by weight, preferably >30% by weight, in particular from 35 to 90% by weight, of an oxidic support having acid centers, at a hot spot temperature of from 240 to 310° C., preferably from 240 to 280° C., and a WHSV over the catalyst of from 0.01 to 1.0, preferably from 0.02 to 1, in particular from 0.05 to 0.5, kg of starting material/l of catalystxhour.
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公开(公告)号:DE10261484A1
公开(公告)日:2004-07-01
申请号:DE10261484
申请日:2002-12-23
Applicant: BASF AG
Inventor: SCHLITTER STEPHAN , HAUBNER MARTIN , ZEHNER PETER , HESSE MICHAEL , WECK ALEXANDER , PINKOS ROLF , GRASLER THOMAS
Abstract: The present invention relates to a process for preparing polytetrahydrofuran, polytetrahydrofuran copolymer, diester or monoester by polymerizing tetrahydrofuran in the presence of at least one telogen and/or comonomer and of an acidic heterogeneous catalyst based on activated sheet silicates or mixed metal oxides in a fluidized bed.
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公开(公告)号:AU2003293663A1
公开(公告)日:2004-06-03
申请号:AU2003293663
申请日:2003-11-06
Applicant: BASF AG
Inventor: SCHUBERT MARKUS , HUBER-DIRR SYLVIA , HESSE MICHAEL , PFEIFER JOCHEN , FISCHER ROLF-HARTMUTH , ROSCH MARKUS , BOTTKE NILS , WECK ALEXANDER , WINDECKER GUNTHER , HEYDRICH GUNNAR
IPC: B01J23/656 , B01J37/02 , C07B41/02 , C07C29/149 , C07C29/17 , B01J23/42
Abstract: A supported catalyst (I) containing 0.1-20 wt.% rhenium and 0.05-10 wt.% platinum (with respect to the total weight of the catalyst) is prepared by: (a) treatment of the optionally pretreated support with a solution of a rhenium compound; (b) drying and heating in a reducing atmosphere at 80-600 degreesC and; (c) impregnation with a solution of a platinum compound and drying. An Independent claim is also included for a process for the production of alcohols by catalytic hydrogenation of carbonyl compounds using the catalyst (I).
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公开(公告)号:DE10243240A1
公开(公告)日:2004-03-25
申请号:DE10243240
申请日:2002-09-17
Applicant: BASF AG
Inventor: ROTERMUND UDO , HEMPEL RENATE , HESSE MICHAEL , RUDLOFF JAN , DESSEIX MARYLINE
Abstract: A foam (I) comprises at least 70 wt.% of carbon with an average cell size of over 20 microns, a porosity of 35-99.5% , over 90% open cells, an internal surface area of over 50 m2/g with cell crosspieces that have a triangular cross-section with inwardly curved sides and pores in the cell framework material of 0.2-50 nm in size and a volume of 0.01-0.8 cm3/g. Independent claims are included for: (1) a powder material (II) prepared by comminution of the foam (I) and; (2) a process for the production of the foam (I) by pyrolysis of a polymer foam, comprising at least 30 wt.% of a polymer material having a nitrogen content of greater than 6 wt.%, porosity of 35-99.5%, open cell content of less than 1% and inorganic materials processed into the foam or applied onto the surface whereby during and/or after pyrolysis the foam treated with water vapor, carbon dioxide and/or oxygen at over 400 degreesC.
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公开(公告)号:DE10225929A1
公开(公告)日:2003-12-24
申请号:DE10225929
申请日:2002-06-11
Applicant: BASF AG
Inventor: ROESCH MARKUS , HESSE MICHAEL , SCHLITTER STEPHAN MARCEL , BOTTKE NILS , FISCHER ROLF HARTMUTH , WECK ALEXANDER , WINDECKER GUNTHER , HEYDRICH GUNNAR , BORCHERT HOLGER , SCHUBERT MARKUS
IPC: C07B61/00 , C07C29/149 , C07C31/20 , C07C29/132 , C07D307/20 , C07D307/32
Abstract: Optionally alkyl-substituted 1,4-butanediol is prepared from C 4 -dicarboxylic acids and/or of derivatives thereof by: a) introducing a gas stream of the C 4 -dicarboxylic acid or the derivative thereof in a first reactor in the gas phase to obtain a product which contains mainly optionally alkyl-substituted gamma-butyro-lactone; b) removing succinic anhydride from the product of step a); c) catalytically hydrogenating the product of step b) in a second reactor in the gas phase to obtain optionally alkyl-substituted 1,4-butanediol; d) removing the desired product from intermediates, by-products and any unconverted reactants; and e) optionally recycling unconverted intermediates into one or both hydrogenation stages. The catalysts employed in each of the hydrogenation stages comprise
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