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公开(公告)号:CA2258797A1
公开(公告)日:1997-12-24
申请号:CA2258797
申请日:1997-06-16
Applicant: BASF AG
Inventor: MEYER GERALD , MUELLER HANS-JOACHIM , KAIBEL GERD , BR CKER FRANZ JOSEF , FLICK KLEMENS , SCHWAB EKKEHARD , FREIRE ERDBRUEGGER CRISTINA , POLANEK PETER
IPC: B01D3/00 , B01D59/32 , B01J8/04 , B01J19/24 , B01J19/32 , B01J23/44 , B01J35/02 , B01J35/06 , B01J37/02 , B01J37/34 , C10G49/00 , C10G49/02
Abstract: The use of a catalyst package which can be produced by the vapour deposition and/or sputtering of at least one substance active as a catalyst and/or promotor on fabrics, knitted materials or foils as substrates in a catalytic distillation process in which a heterogeneous-catalytic reaction is combined with simultaneous distillation or rectification on the catalyst package.
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公开(公告)号:AU6820296A
公开(公告)日:1997-03-12
申请号:AU6820296
申请日:1996-08-08
Applicant: BASF AG
Inventor: JACHOW HARALD , SCHWAB EKKEHARD , KORMANN CLAUDIUS , DAUSCH WILMA , SPERLING KARIN , WESTENFELDER HORST
IPC: A61K8/19 , A61K8/00 , A61K8/04 , A61K8/26 , A61K8/29 , A61Q17/04 , A61Q19/00 , C01G23/053 , C09C1/36 , A61K7/00
Abstract: PCT No. PCT/EP96/03504 Sec. 371 Date Feb. 12, 1998 Sec. 102(e) Date Feb. 12, 1998 PCT Filed Aug. 8, 1996 PCT Pub. No. WO97/07058 PCT Pub. Date Feb. 27, 1997Titanium dioxide pigments are obtainable by complete hydrolysis of a hydrolyzable titanium compound at from 0 to 100 DEG C. with intensive stirring and with setting of a pH in the range from 3 to 8 and maintenance of this pH within a range of 0.3 units. The titanium dioxide pigments can be employed for the production of cosmetic preparations and medicaments.
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公开(公告)号:FI970789A
公开(公告)日:1997-02-25
申请号:FI970789
申请日:1997-02-25
Applicant: BASF AG
Inventor: KORMANN CLAUDIUS , SCHWAB EKKEHARD , SCHLEGEL REINHOLD
IPC: A61B5/055 , A61K49/18 , C01G49/06 , C01G49/08 , C09C1/24 , C09D17/00 , G01R33/28 , G11B5/706 , C09C
Abstract: PCT No. PCT/EP95/03230 Sec. 371 Date Feb. 18, 1997 Sec. 102(e) Date Feb. 18, 1997 PCT Filed Aug. 16, 1995 PCT Pub. No. WO96/06891 PCT Pub. Date Mar. 7, 1996 gamma -Fe2O3 pigments and Fe3O4 pigments with a particle diameter of 2 to 100 nm, a saturation magnetization above 40 nTm3/g, a remanence below 10 nTm3/g, a Cr content below 40 mg/kg of pigment, a Cu content below 40 mg/kg of pigment and C content below 100 mg/kg of pigment and aqueous suspension of these pigments. The pigments are used in aqueous suspension in the medical sector, in particular as contrast agents in magnetic resonance imaging.
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公开(公告)号:AT380231T
公开(公告)日:2007-12-15
申请号:AT02020725
申请日:2002-09-14
Applicant: BASF AG
Inventor: KOCH MICHAEL , SCHWAB EKKEHARD , TRUEBENBACH PETER , SCHAEFER HARALD
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公开(公告)号:DE102005008613A1
公开(公告)日:2006-08-31
申请号:DE102005008613
申请日:2005-02-23
Applicant: BASF AG
Inventor: VANOPPEN DOMINIC , LAAR FREDERIK VAN , BEUERMANN THOMAS , KRUG GEORG , OEHLENSCHLAEGER STEFFEN , SCHWAB EKKEHARD , VOS HARTWIG , MORGENSCHWEIS KONRAD , PENZEL ULRICH , TITTELBACH-HELMRICH DIETRICH
IPC: C07C209/36 , B01J4/02 , C07B43/04 , C07C209/82 , C07C211/51 , C07C213/02 , G01N21/31
Abstract: Preparation of aromatic amines or aliphatic amino alcohols comprises hydrogenating nitro-aromatic compounds or nitro alcohols, respectively in the presence of a catalyst, separating the catalysts from fluid amine- or amino alcohols containing reaction mixture, in a reactor, and measuring the absorption of UV/visible-radiation by the reaction mixture to determine the concentration of nitro and nitroso compounds. An independent claim is included for a device for executing the preparation of aromatic amines or aliphatic amino alcohols.
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公开(公告)号:DE10150556A1
公开(公告)日:2003-04-17
申请号:DE10150556
申请日:2001-10-15
Applicant: BASF AG
Inventor: KOCH MICHAEL , SCHWAB EKKEHARD , TRUEBENBACH PETER , SCHAEFER HARALD
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公开(公告)号:DE10149631A1
公开(公告)日:2003-04-10
申请号:DE10149631
申请日:2001-10-09
Applicant: BASF AG
Inventor: HILL THOMAS , HAAKE MATHIAS , SCHWAB EKKEHARD , FRENZEL ANDREA , WOERZ HELMUT
Abstract: Selective catalytic gas-phase hydrogenation of alkynes, dienes, alkenynes and/or polyenes in an olefin-containing hydrocarbon stream in a series of two or more reaction zones without feeding part of the hydrocarbon stream between the penultimate and last reaction zones. The process comprises adjusting the hydrogen content before the penultimate zone and the conversion in the penultimate zone so that the reaction mixture leaving the penultimate zone contains at least 0.7 vol.% hydrogen.
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公开(公告)号:DE10142635A1
公开(公告)日:2003-03-20
申请号:DE10142635
申请日:2001-08-31
Applicant: BASF AG
Inventor: FUNKE FRANK , HILL THOMAS , MELDER JOHANN-PETER , SCHWAB EKKEHARD , HIMMEL WALTER , HENKES ERHARD , PETERSEN HERMANN , KOERNER REINHARD
IPC: B01J23/40 , B01J23/70 , B01J23/75 , B01J23/889 , B01J23/89 , B01J27/185 , B01J27/187 , B01J35/10 , B01J37/00 , B01J37/03 , B01J37/08 , B01J37/18 , C07B61/00 , C07C209/26 , C07C209/48 , C07C211/36 , C07C253/30 , C07C255/61
Abstract: The invention relates to a method for the production of 3-aminomethyl-3,5,5-trimethylcyclohexylamine (isophorondiamine, IPDA) with a cis/trans isomer ratio of at least 70/30 from 3-cyano-3,5,5-trimethylcyclohexanon (isophorone nitril, IPN), NH3 and H2, wherein hydrogenation is carried out in the presence of a hydrogenation catalyst at temperatures ranging from 50 to 200 DEG C and at a pressure ranging from 50 to 300 bar. The invention is characterized in that the alkali metal content of the hydrogenation catalyst is
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公开(公告)号:CA2414989A1
公开(公告)日:2003-01-02
申请号:CA2414989
申请日:2001-07-02
Applicant: BASF AG
Inventor: SCHWAB EKKEHARD , STEINBRENNER ULRICH , LINDEN GERD , COX GERHARD , TENTEN ANDREAS , BOHNER GERD , SIGWART CHRISTOPH , HIBST HARTMUT , FISCHER ROLF-HARTMUTH , HESSE MICHAEL , HAUBNER MARTIN , NARBESHUBER THOMAS
IPC: C08G65/10 , B01J21/06 , B01J23/28 , B01J23/30 , B01J27/188 , B01J35/00 , B01J35/10 , B01J37/00 , C08G65/20 , C08G65/26 , B01J23/20 , B01J23/24
Abstract: The invention relates to a catalyst which contains a catalytically active quantity of at least one oxygen-containing molybdenum and/or wolfram compound on an oxidic support material and which has been calcinated at temperatures of 400 to 900° C. after the precursor compound of the catalytically active compounds have been applied to the support material or to a support material precursor. The transport pores for this catalyst each have a diameter of >25 nm and a volume of at least 50 mm /g. The catalyst contains x mumol (wolfram and/or molybdenum)/m molybdenum and/or wolfram, with 10.1 /g. Catalysts of this type are characterized by an acidity of at least 70 mumol/g at pKs
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公开(公告)号:DE10124600A1
公开(公告)日:2002-11-28
申请号:DE10124600
申请日:2001-05-21
Applicant: BASF AG
Inventor: VANOPPEN DOMINIC , SCHWAB EKKEHARD , MUELLER JOERN , PENZEL ULRICH , GEORGI GUNTER , WEIDNER BERND , TITTELBACH-HELMRICH DIETRICH , DAHLHAUS JUERGEN
IPC: B01J23/76 , B01J21/06 , B01J23/755 , B01J23/78 , B01J23/83 , B01J35/10 , B01J37/03 , B01J37/16 , C07B61/00 , C07C209/36 , C07C211/46 , C07C211/47 , C07C211/50 , C07C211/51 , C07C211/44
Abstract: Production of a supported nickel catalyst involves co-precipitating nickel and at least one other metal (M), selected from silicon, zirconium, hafnium, alkaline earth metals, yttrium, lanthanum and cerium, and optionally a Group 5-11 metal dopant, from a solution containing the corresponding metal salts onto a particulate titania (TiO2) support, and drying, calcining, reducing and optionally passivating the product. An Independent claim is included for a process in which the above catalyst is used.
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