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公开(公告)号:NO20003933D0
公开(公告)日:2000-08-03
申请号:NO20003933
申请日:2000-08-03
Applicant: BASF AG
Inventor: HEINEKE DANIEL , HARTH KLAUS , STABEL UWE
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公开(公告)号:ES2097051T3
公开(公告)日:1997-03-16
申请号:ES94918352
申请日:1994-05-20
Applicant: BASF AG
Inventor: STABEL UWE , WOERZ HELMUT , KOTKAMP RUEDIGER , FRIED ANDREAS
Abstract: PCT No. PCT/EP94/01647 Sec. 371 Date Nov. 17, 1995 Sec. 102(e) Date Nov. 17, 1995 PCT Filed May 20, 1994 PCT Pub. No. WO95/03375 PCT Pub. Date Feb. 2, 1995A process for recycling plastic waste in a steam cracker, wherein a melt obtained from plastic waste is converted into products at from 400 DEG 550 DEG C., and a distillate fraction is separated off from the products at from 180 DEG to 280 DEG C. and is fed as feed material to a steam cracker.
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公开(公告)号:CA2151602A1
公开(公告)日:1994-06-23
申请号:CA2151602
申请日:1993-12-02
Applicant: BASF AG
Inventor: STABEL UWE , WUNSCH GERD , WOERZ HELMUT , FRIED ANDREAS , KOTKAMP RUEDIGER
IPC: C07C7/00 , C07C7/04 , C07C13/465 , C07C15/44 , C07C15/46 , C08J11/14 , C08L25/02 , C10G7/00 , C10G9/00 , C10G70/04
Abstract: The invention concerns a method of obtaining, from the cracked gases emerging from a steam cracker, a polymerizable fraction of recyclable material consisting of styrene, methylstyrenes, vinyltoluenes, indene, methylindenes and fractions whose boiling points lie between those of styrene and the methylindenes, a secondary stream from the cracked-gas column being divided, by means of a distillation unit, into the fraction of recyclable material and into fractions which are fed back to the cracked gas column.
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公开(公告)号:DE4111071A1
公开(公告)日:1992-10-08
申请号:DE4111071
申请日:1991-04-05
Inventor: BOELT HEINZ , WALSER FRANZ , FRITZ PETER MATTHIAS , WUNSCH GERD , STABEL UWE
IPC: C07C5/32
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公开(公告)号:CA2432200C
公开(公告)日:2007-06-26
申请号:CA2432200
申请日:2000-12-22
Applicant: BASF AG
Inventor: HEINEKE DANIEL , STABEL UWE , HARTH KLAUS
IPC: B01J35/10 , B01J21/06 , B01J23/02 , B01J23/08 , B01J23/62 , B01J23/70 , B01J35/04 , B01J37/00 , C07B61/00 , C07C5/32 , C07C5/333 , C07C11/02
Abstract: Catalysts with bimodal pore radius distribution, comprising a) 10 to 99.9 wt . % zirconium dioxide, b) 0 to 60 wt. % aluminium oxide, silicon dioxide and/or titanium dioxide and c) 0.1 to 10 wt. % of at least one element of the first or second main group, an element of the third sub-group, an element of the eighth sub-group of the periodic element system, lanthanum and/or zinc, with the proviso that the total of the weight percentages is 100.
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公开(公告)号:NO320582B1
公开(公告)日:2005-12-27
申请号:NO20003936
申请日:2000-08-03
Applicant: BASF AG
Inventor: HEINEKE DANIEL , HARTH KLAUS , STABEL UWE
Abstract: Catalysts (I) with a bimodal pore radius distribution and a BET surface of more than 70 m /g, containing or consisting mainly of (a) 10-99.9 wt% zirconium dioxide, (b) 0-60 wt% aluminum oxide, silicon dioxide and/or titanium dioxide and (c) 0.1-10 wt% Main Group 1 or 2 element(s), Sub-Group 3 element(s), Sub-Group 8 element(s), lanthanum and/or tin. Independent claims are also included for (i) a process for the production of (I) by mixing the catalyst components with 2-30 wt% polyamine, polyacrylate, poly-alcohol, polysiloxane and/or carbohydrate, or especially polyvinylpyrrolidone, and then calcining at above 550 degrees C; (ii) a process for the dehydrogenation of 2-16C hydrocarbons in presence of (I) and optionally in presence of water vapor.
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公开(公告)号:BR0017392A
公开(公告)日:2004-02-03
申请号:BR0017392
申请日:2000-12-22
Applicant: BASF AG
Inventor: HEINEKE DANIEL , HARTH KLAUS , STABEL UWE
IPC: B01J21/06 , B01J23/62 , B01J35/04 , B01J35/10 , C07B61/00 , C07C5/32 , C07C5/333 , C07C11/02 , B01J23/02 , B01J23/70 , B01J37/00 , B01J23/08
Abstract: Catalysts with bimodal pore radius distribution, comprising a) 10 to 99.9 wt. % zirconium dioxide, b) 0 to 60 wt. % aluminium oxide, silicon dioxide and/or titanium dioxide and c) 0.1 to 10 wt. % of at least one element of the first or second main group, an element of the third sub-group, an element of the eighth sub-group of the periodic element system, lanthanum and/or zinc, with the proviso that the total of the weight percentages is 100.
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公开(公告)号:DE10130670A1
公开(公告)日:2003-01-23
申请号:DE10130670
申请日:2001-06-28
Applicant: BASF AG
Inventor: STABEL UWE , BIRNBAUM EBERHARD , RIZK FARID , SCHLICHTHAERLE GOTTFRIED
Abstract: The invention relates to the implementation of heterogeneous catalytic reactions in a moving-bed reactor. Expansion volumes for the catalyst are provided in the defining walls of the catalyst bed, said volumes being easily created by means of at least two graduated conical-or polygonal-frustrum-shaped walls. Said implementation reduces the catalyst abrasion and avoids damaging the catalyst screens.
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公开(公告)号:BR0103915A
公开(公告)日:2001-12-18
申请号:BR0103915
申请日:2001-01-10
Applicant: BASF AG
Inventor: ZEHNER PETER , MACHHMMER OTTO , HECHLER CLAUS , WECK ALEXANDRE , OLBERT ERHARD , STABEL UWE
IPC: F28F3/00 , B01J8/02 , B01J19/24 , B01J35/04 , C07C51/215 , C07C57/145 , C07D307/60
Abstract: A process for the preparation of maleic anhydride by heterogeneously catalyzed gas-phase oxidation in a reactor with feed for the reaction mixture at one end of the reactor and discharge of the product mixture at the opposite end of the reactor, and with devices for dissipating the heat of reaction which are arranged in the reactor interior and through which a heat-exchange medium flows and which are designed as heat-exchanger plates.
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公开(公告)号:DE19952964A1
公开(公告)日:2001-05-10
申请号:DE19952964
申请日:1999-11-03
Applicant: BASF AG
Inventor: HECHLER CLAUS , MACHHAMMER OTTO , OLBERT GERHARD , STABEL UWE , ZEHNER PETER
IPC: B01J8/02 , B01J19/24 , C07B61/00 , C07C27/00 , C07C45/33 , C07C45/35 , C07C45/37 , C07C47/22 , C07C51/235 , C07C57/05 , C07C57/055 , F28D9/00 , C07C45/27
Abstract: The invention relates to a method for the continuous gas phase oxidation of C3- and C4-precursors to (meth)acrolein and/or (meth)acrylic acid in the presence of a catalyst, in a reactor. Said reactor has a feed element for the reaction mixture at one reactor end and a discharge element for the reaction mixture at the opposite reactor end and is equipped with devices for dissipating the reaction heat inside the reactor. A heat exchanger agent flows through said devices, which are configured in the form of heat exchanger plates.
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