公开(公告)号：ES2116791T3

公开(公告)日：1998-07-16

申请号：ES96100461

申请日：1996-01-13

Applicant: BASF AG

Inventor： HERBST HOLGER DR ,  HAMMON ULRICH DR

IPC: C07C51/44 ,  C07C57/04 ,  C07C57/07

Abstract: In the sepn. of (meth)acrylic acid (I) from mixts. contg. (I) as main prod. and lower aldehydes as by-prods. by rectification in a column with a distn. zone and a concn. zone, the mixt. is not supplied to the column directly. Instead, it is passed to a heated dwell vessel connected to the concn. zone, in which the mixt. is kept boiling, and the sump liquid from this vessel is fed to the column.

公开(公告)号：DE19536179A1

公开(公告)日：1997-04-03

申请号：DE19536179

申请日：1995-09-28

Applicant: BASF AG

Inventor： HAMMON ULRICH DR ,  SCHLIEPHAKE VOLKER DR ,  PIES WOLFGANG DR ,  RAUH ULRICH

IPC: C07B63/00 ,  C07C51/44 ,  C07C57/04 ,  C07C57/07

Abstract: A process for the rectification and sepn. of unsatd. carboxylic acids (I) from the solvents in which (I) are absorbed after the synthesis reaction. The process involves interrupting the rectification and flushing out the rectification column with basic soln.

公开(公告)号：CZ9601128A3

公开(公告)日：1996-09-11

申请号：CZ112896

申请日：1994-10-11

Applicant: BASF AG

Inventor： TENTEN ANDREAS DR ,  HAMMON ULRICH DR ,  WEIDLICH PETER DR

IPC: B01J23/00 ,  B01J23/28 ,  B01J23/88 ,  B01J23/887 ,  B01J23/888 ,  B01J37/00 ,  B01J37/02 ,  B01J37/08 ,  C07B33/00 ,  C07B35/04 ,  C07C51/25 ,  C07C57/04 ,  C07C57/055 ,  C07C253/26 ,  B01J37/10

CPC classification number: C07C51/252 ,  B01J23/002 ,  B01J23/28 ,  B01J23/88 ,  B01J23/8877 ,  B01J23/8885 ,  B01J37/0045 ,  B01J37/0223 ,  B01J37/08 ,  B01J2523/00 ,  C07B33/00 ,  C07B35/04 ,  C07C57/04 ,  B01J2523/17 ,  B01J2523/55 ,  B01J2523/69

公开(公告)号：CZ9502294A3

公开(公告)日：1996-03-13

申请号：CZ229495

申请日：1995-09-07

Applicant: BASF AG

Inventor： RUPPEL WILHELM DR ,  WEGERLE ULRIKE ,  TENTEN ANDREAS DR ,  HAMMON ULRICH DR

IPC: B01J23/28 ,  B01J8/06 ,  B01J21/02 ,  B01J23/16 ,  C07B61/00 ,  C07C51/25 ,  C07C57/055

CPC classification number: B01J8/067 ,  B01J2208/00212 ,  C07C51/252 ,  C07C57/04

公开(公告)号：DE59100424D1

公开(公告)日：1993-11-04

申请号：DE59100424

申请日：1991-07-03

Applicant: BASF AG

Inventor： BOEHNING KARL-HEINZ DR ,  DUEMBGEN GERD DR ,  HAMMON ULRICH DR ,  KRABETZ RICHARD DR ,  MERGER FRANZ DR ,  SCHWARZMANN MATHIAS DR ,  THIESSEN FRITZ DR ,  VOGEL HERBERT DR

IPC: B01J27/19 ,  B01J27/053 ,  B01J27/198 ,  B01J27/199 ,  C07B61/00 ,  C07C51/25 ,  C07C57/04 ,  C07C57/055

Abstract: Masses of the general formula I… Mo12PaVbX cX dX eSbfRegShOn (I),… in which the variables are defined as follows:… X potassium, rubidium and/or caesium,… X copper and/or silver,… X cerium, boron, zirconium, manganese and/or bismuth,… a 0.5 to 3.0… b 0.01 to 3.0… c 0.2 to 3.0… d 0.01 to 2.0… e 0 to 2.0… f 0.01 to 2.0… g 0 to 1.0… h 0.001 to 0.5 and… n a number which is determined by the valency and frequency of the elements other than oxygen in I. … These masses are suitable as catalysts for the production of methacrylic acid by catalytic gas-phase oxidation of methacrolein.

公开(公告)号：CZ9202974A3

公开(公告)日：1993-04-14

申请号：CS297492

申请日：1992-09-29

Applicant: BASF AG

Inventor： HAMMON ULRICH DR ,  HERZOG KLAUS DR ,  NEUMANN HANS-PETER DR

IPC: C07C51/235 ,  B01J27/186 ,  B01J27/188 ,  B01J27/19 ,  B01J27/195 ,  B01J27/199 ,  C07C51/25 ,  C07C57/055

CPC classification number: C07C51/252 ,  C07C57/04

公开(公告)号：DE4132263A1

公开(公告)日：1993-04-01

申请号：DE4132263

申请日：1991-09-27

Applicant: BASF AG

Inventor： HAMMON ULRICH DR ,  HERZOG KLAUS DR ,  NEUMANN HANS-PETER DR

IPC: C07C51/235 ,  C07C51/25 ,  C07C57/055

Abstract: A method for the catalytic gas-phase oxidation of acrolein to acrylic acid in a contact tubular solid bed reactor at elevated temperature on catalytically active oxides with a conversion of the acrolein on a single pass of >/= 95%, in which the reaction temperature in the flow direction along the contact tube in a first reaction zone from entry of the exit reaction gases containing the reactants into the contact tube until a conversion of the acrolein of 20 to 40% is achieved is 260 to 300 DEG C and in which subsequently thereto the reaction temperature is decreased abruptly or in successive steps or continuously along the contact tube until an acrolein conversion of >/= 95% is achieved by a total of 5 to 40 DEG C with the proviso that the reaction temperature in this second reaction zone is not less than 240 DEG C.

公开(公告)号：MY139893A

公开(公告)日：2009-11-30

申请号：MYPI20032258

申请日：2003-06-17

Applicant: BASF AG

Inventor： HAMMON ULRICH DR ,  MESCHKE JOCHEN DR ,  RAUH ULRICH ,  MUELLER-ENGEL KLAUS JOACHIM DR ,  SCHLEMMER PETER DR ,  SCHLIEPHAKE VOLKER DR

IPC: B01J4/00 ,  C07C51/16 ,  C07B61/00 ,  C07C45/33 ,  C07C45/34 ,  C07C45/35 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C57/05

Abstract: A CONTINUOUSLY OPERATED HETEROGENEOUSLY CATALYZED GAS-PHASE PARTIAL OXIDATION OF AT LEAST ONE ORGANIC COMPOUND IN AN OXIDATION REACTOR IS OPERATED SAFELY BY A PROCESS IN WHICH AN EXPLOSION DIAGRAM FOR THE FEED GAS MIXTURE IS DEPOSITED AS THE BASIC OF A CUT-OUT MECHANISM IN A COMPUTER.

公开(公告)号：MY139283A

公开(公告)日：2009-09-30

申请号：MYPI20052014

申请日：2005-05-05

Applicant: BASF AG

Inventor： DIETERLE MARTIN DR ,  EGER KNUT DR ,  MUELLER-ENGEL KLAUS JOACHIM DR ,  HAMMON ULRICH DR ,  SCHLIEPHAKE VOLKER DR

IPC: B01J8/00 ,  B01J8/06

Abstract: A METHOD OF CHARGING CATALYST TUBES OF A BUNDLE OF CATALYST TUBES IN A STRUCTURED FASHION, IN WHICH UNIFORMLY PREDISPENSED PORTIONS OF FORMULATIONS OF SHAPED CATALYST BODIES ARE USED FOR PRODUCING A SECTION OF CHARGE.

公开(公告)号：MY128141A

公开(公告)日：2007-01-31

申请号：MYPI20013043

申请日：2001-06-27

Applicant: BASF AG

Inventor： KROKOSZINSKI ROLAND DR ,  HAMMON ULRICH DR ,  TODD KEVIN DR

IPC: C07C27/10 ,  C07B61/00 ,  C07C27/14 ,  C07C45/33 ,  C07C45/35 ,  C07C45/50 ,  C07C47/02 ,  C07C47/22 ,  C07C51/215 ,  C07C51/235 ,  C07C51/25 ,  C07C57/05 ,  C07C57/055

Abstract: A PROCESS FOR PREPARING HYDROFORMYLATION PRODUCTS OF PROPYLENE AND FOR PREPARING ACRYLIC ACID AND/OR ACROLEIN COMPRISES A) FEEDING A PROPYLENE-CONTAINING FEED IN WHICH FROM 2 TO 40BY WEIGHT OF PROPANE IS PRESENT AND ALSO CARBON MONOXIDE AND HYDROGEN INTO A REACTION ZONE AND REACTING THIS MIXTURE IN THE PRESENCE OF A HYDROFORMYLATION CATALYST TO FORM HYDROFORMYLATION PRODUCTS OF PROPANE, B) SEPARATING A STREAM CONSISTING ESSENTIALLY OF UNREACTED PROPYLENE AND PROPANE FROM THE OUTPUT FROM THE REACTION ZONE, AND C) SUBJECTING THE STREAM CONSISTING ESSENTIALLY OF PROPYLENE AND PROPANE TO A CATALYTIC GAS-PHASE OXIDATION IN THE PRESENCE OF MOLECULAR OXYGEN TO FORM ACRYLIC ACID AND/OR ACROLEIN.