公开(公告)号：AT378107T

公开(公告)日：2007-11-15

申请号：AT02027073

申请日：2002-12-03

Applicant: BASF AG

Inventor： GERLACH TILL ,  GOEBBEL HANS-GEORG ,  FUNKE FRANK ,  EBEL KLAUS ,  SCHWAB EKKEHARD ,  UNVERRICHT SIGNE ,  KOERNER REINHARD ,  LOBREE LISA

IPC: B01J23/89 ,  B01J21/18 ,  B01J33/00 ,  B01J37/03 ,  C07B61/00 ,  C07C29/141 ,  C07C29/145 ,  C07C29/17 ,  C07C33/02 ,  C07C33/025

公开(公告)号：DE10330934A1

公开(公告)日：2005-02-17

申请号：DE10330934

申请日：2003-07-08

Applicant: BASF AG

Inventor： SALDEN AXEL ,  LANZENDOERFER FRANZ ,  UNVERRICHT SIGNE

IPC: B01D3/14 ,  C07C45/82 ,  C07C47/21

Abstract: A method for the continuous isolation of citronellal or citronellol from crude mixtures involves rectification in a partition-wall column with upper and lower combining column sections, a side feed inlet and a side take-off for the pure product. A rectification method for the continuous isolation of citronellal (I) or citronellol (II) from a crude mixture containing at least one of these compounds, involves (a) feeding the mixture into the side of a feeder column (3, 4) with a concentrating section (3) above the feed inlet (9) and a stripper section (4) below (9), (b) providing an upper combining column (2) communicating with the top of section (3) and fitted with a condenser (12) at the top of (2), plus another combining column (7) with a heater (14) at the bottom of the stripper (4), (c) providing a take-off column (5, 6) which communicates with columns (2) and (7), and (d) taking off (I) or (II) as a side product from column (5, 6), plus low-boilers from the top of column (2) and high-boilers from the bottom of column (7).

公开(公告)号：ES2213002T3

公开(公告)日：2004-08-16

申请号：ES00918748

申请日：2000-02-28

Applicant: BASF AG

Inventor： UNVERRICHT SIGNE ,  ARNOLD HEIKO ,  TENTEN ANDREAS ,  HAMMON ULRICH ,  NEUMANN HANS-PETER ,  HARTH KLAUS

IPC: B01J23/00 ,  B01J23/31 ,  B01J23/88 ,  B01J23/887 ,  B01J35/00 ,  C07B61/00 ,  C07C45/35 ,  C07C51/215 ,  C07C51/25 ,  C07C57/04 ,  C07C57/05

Abstract: A process for the catalytic gas-phase oxidation of propene to acrylic acid, in which the reaction gas starting mixture is oxidized, with a high propene loading, in a first reaction stage, over a first fixed-bed catalyst which is housed in two successive reaction zones A, B, the reaction zone B being kept at a higher temperature than the reaction zone A, and the acrolein-containing product gas mixture of the first reaction stage is then oxidized in a second reaction stage, with a high acrolein loading, over a second fixed-bed catalyst which is housed in two successive reaction zones C, D, the reaction zone D being kept at a higher temperature than the reaction zone C.

公开(公告)号：DE50102496D1

公开(公告)日：2004-07-08

申请号：DE50102496

申请日：2001-10-09

Applicant: BASF AG

Inventor： PETZOLDT JOCHEN ,  UNVERRICHT SIGNE ,  ARNOLD HEIKO

IPC: B01J23/88 ,  B01J23/887 ,  B01J35/10 ,  B01J37/00 ,  B01J37/02 ,  C07B61/00 ,  C07C45/35 ,  C07C47/22

Abstract: Coated catalysts which are suitable for the gas-phase catalytic oxidation of propene to acrolein are prepared by a process in which rings are used as supports and water is used as a binder.

公开(公告)号：DE50102489D1

公开(公告)日：2004-07-08

申请号：DE50102489

申请日：2001-09-20

Applicant: BASF AG

Inventor： UNVERRICHT SIGNE ,  FELDER RAIMUND ,  ARNOLD HEIKO ,  PETZOLDT JOCHEN

IPC: C01B13/14 ,  B01J23/30 ,  B01J23/88 ,  B01J23/887 ,  B01J35/00 ,  B01J37/00 ,  B01J37/03 ,  C07B61/00 ,  C07C51/235 ,  C07C51/25 ,  C07C57/04 ,  C07C57/055

Abstract: In a process for preparing a multiplephase multimetal oxide composition comprising Mo, V, Cu and, if desired, further elements, at least one phase is preformed separately and dispersed in a plastically deformable precursor composition of a further phase. The mixture is dried and calcined. The multimetal oxide composition is suitable as active composition of catalysts for the catalytically oxidation of organic compounds in the gas phase, in particular for the oxidation of acrolein to acrylic acid.

公开(公告)号：ES2209832T3

公开(公告)日：2004-07-01

申请号：ES00910722

申请日：2000-02-28

Applicant: BASF AG

Inventor： UNVERRICHT SIGNE ,  ARNOLD HEIKO ,  TENTEN ANDREAS ,  HAMMON ULRICH

IPC: B01J8/02 ,  B01J8/04 ,  B01J23/88 ,  B01J8/06 ,  B01J23/887 ,  B01J37/02 ,  C07B61/00 ,  C07C51/235 ,  C07C51/25 ,  C07C57/04 ,  C07C57/055

Abstract: In a process for the catalytic gas-phase oxidation of acrolein to acrylic acid, the reaction gas starting mixture is passed, with an acrolein loading of >=150 l (s.t.p.)/l.h, over a fixed-bed catalyst which is housed in two spatially successive reaction zones A, B, the reaction zone B being kept at a higher temperature than the reaction zone A.

公开(公告)号：ES2208289T3

公开(公告)日：2004-06-16

申请号：ES00912516

申请日：2000-02-28

Applicant: BASF AG

Inventor： UNVERRICHT SIGNE ,  ARNOLD HEIKO ,  TENTEN ANDREAS ,  HAMMON ULRICH ,  NEUMANN HANS-PETER ,  HARTH KLAUS

IPC: B01J23/88 ,  B01J23/00 ,  B01J23/31 ,  B01J23/887 ,  B01J35/00 ,  C07B61/00 ,  C07C27/14 ,  C07C45/35 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C57/04 ,  C07C57/05

Abstract: A process for the catalytic gas-phase oxidation of propene to acrylic acid, in which the reaction gas starting mixture is oxidized, with an increased propene loading, in a first reaction stage, over a first fixed-bed catalyst and then the acrolein-containing product gas mixture of the first reaction stage is oxidized, in a second reaction stage, with an increased acrolein loading, over a second fixed-bed catalyst, the catalyst moldings in both reaction stages having an annular geometry.

公开(公告)号：DE10223974A1

公开(公告)日：2003-12-11

申请号：DE10223974

申请日：2002-05-29

Applicant: BASF AG

Inventor： GOEBBEL HANS-GEORG ,  KAIBEL GERD ,  RUST HARALD ,  UNVERRICHT SIGNE

IPC: C07C29/80 ,  C11B9/02 ,  A61K7/46 ,  B61D3/14 ,  C07C33/02 ,  C07C33/03

Abstract: Continuous isolation of 2 stereoisomeric isoprenoid alcohols (IA, IB) from crude mixture by rectification involves feeding crude mixture into side of feed column coupled with discharge column(s) and discharging (IA) and (IB) from discharge column(s), columns being coupled in such way that there is no cross-mixing of vapor and condensate between feed column and discharge column(s), at least in (I) discharge region.

公开(公告)号：DE50004251D1

公开(公告)日：2003-12-04

申请号：DE50004251

申请日：2000-02-28

Applicant: BASF AG

Inventor： ARNOLD HEIKO ,  UNVERRICHT SIGNE ,  HAMMON ULRICH ,  NEUMANN HANS-PETER ,  HARTH KLAUS ,  TENTEN ANDREAS

IPC: B01J23/88 ,  B01J8/02 ,  B01J8/04 ,  B01J8/06 ,  B01J23/00 ,  B01J23/31 ,  B01J23/887 ,  B01J35/00 ,  C07B61/00 ,  C07C27/14 ,  C07C45/35 ,  C07C47/22 ,  C07C51/21 ,  C07C51/25 ,  C07C57/04 ,  C07C57/05 ,  C07C57/055

Abstract: In a process for the catalytic gas-phase oxidation of propene to acrolein, the reaction gas starting mixture is passed with a propene loading of >=160 l(S.T.P.)/l.h over a fixed-bed catalyst which is housed in two spatially successive reaction zones A,B, the reaction zone B being kept at a higher temperature than the reaction zone A.

公开(公告)号：AU2002358592A1

公开(公告)日：2003-06-17

申请号：AU2002358592

申请日：2002-12-04

Applicant: BASF AG

Inventor： HAESE FRANK ,  EBEL KLAUS ,  BURKART KIRSTEN ,  UNVERRICHT SIGNE ,  MUNSTER PETER

IPC: C07B61/00 ,  C07C29/56 ,  C07C33/02 ,  C07C33/03

Abstract: The present invention relates to a process for isomerizing reactant allyl alcohols to product allyl alcohols in the presence of a catalyst, wherein the reactant allyl alcohol is rearranged to product allyl alcohol in semicontinuous or continuous mode in a catalyst-containing suitable reactor. In particular, the process according to the invention is used to prepare linalool from Geraniol and/or nerol.