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公开(公告)号:DE19746279A1
公开(公告)日:1999-04-22
申请号:DE19746279
申请日:1997-10-20
Applicant: BASF AG
Inventor: QUEISSER JOACHIM DR , SLANY MICHAEL DR , LUDWIG ALFONS DR
IPC: B01J31/16 , B01J31/18 , B01J31/24 , B01J37/03 , C07F9/50 , C07F15/00 , C08G67/02 , C08J5/00 , C08J5/04 , C08J5/18 , C08L73/00 , D01F6/96
Abstract: A supported catalyst for the production of carbon monoxide copolymers is obtained by suspending the support in non-polar aprotic solvent, adding a solution of a Group VIIIB, IB or IIB metal complex with bi- or tri-dentate ligand(s) in a polar aprotic solvent, possibly adding non- polar solvent and working up by filtration. A process for the production of linear alternating copolymers of carbon monoxide (CO) and olefinically unsaturated compounds uses an activator compound and a supported heterogeneous catalyst system, which is obtained by: (a) suspension of the support material in a non-polar aprotic liquid (NPAL), (b) controlled addition of a Group VIIIB, IB or IIB metal chelate complex with bi- or tri- dentate ligand(s) as a solution in a polar aprotic liquid, (c) filtration, optionally followed by washing with NPAL and (d) optionally removing liquid residues with inert gas. Alternatively, the mixture obtained from stage (b) may be mixed with NPAL before performing stages (c) and (d) as above. An Independent claim is also included for carbon monoxide copolymers obtained by this process.
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公开(公告)号:DE19752181A1
公开(公告)日:1999-05-27
申请号:DE19752181
申请日:1997-11-25
Applicant: BASF AG
Inventor: HUENGER HANS-HARALD , LUDWIG ALFONS DR , NEUBERG RAINER DR , PIPPER GUNTER , SAUER THOMAS DR , WILMS AXEL DR
Abstract: Preparation of polyamides from a lactam(s) and optionally other monomers and additives and fillers comprises: (a) concentrating the extraction water from the extraction of polyamide to at most 85%; (b) adjusting the water content to 0.5-13 wt.% by adding fresh lactam; (c) exposing to polyamide forming conditions; and (d) adiabatically expanding during polymerization to reduce the water content.
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公开(公告)号:DE19752183A1
公开(公告)日:1999-05-27
申请号:DE19752183
申请日:1997-11-25
Applicant: BASF AG
Inventor: ERBES JOERG DR , LUDWIG ALFONS DR , PIPPER GUNTER
IPC: C08J3/12 , B01D11/02 , B29B9/16 , C08G69/00 , C08G69/04 , C08G69/16 , C08G69/46 , C08G69/14 , C08L77/02 , B01D11/00
Abstract: Continuous extraction of polyamide particles with an aqueous extraction medium in an essentially vertical extraction column comprises using subdivided extraction columns in two zones, with extraction in the first zone with 40-95 wt.% aqueous caprolactam and in the second zone with water. An Independent claim is included for an extraction column for use in the above process comprising a first zone (2) with a means for adding and removing an extraction medium and a second zone (3), where the ratio of length of zone 1 to zone 2 is 1:5-5:1 and of diameter is 8-2:1.
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公开(公告)号:DE19746280A1
公开(公告)日:1999-04-22
申请号:DE19746280
申请日:1997-10-20
Applicant: BASF AG
Inventor: QUEISSER JOACHIM DR , SLANY MICHAEL DR , LUDWIG ALFONS DR
IPC: B01J31/22 , B01J31/16 , B01J31/18 , B01J31/24 , B01J37/02 , B01J37/03 , C08F2/18 , C08F2/34 , C08F4/02 , C08F4/42 , C08F10/00 , C08G67/02
Abstract: Supported transition metal catalysts are obtained by suspending the support material in a non-polar aprotic solvent, adding a solution of a Group VIIIB, IB or IIB metal complex with bi- or tri-dentate ligand(s) in a polar aprotic solvent, possibly adding non-polar solvent and working up by filtration. A process for the production of supported transition metal catalysts comprises: (a) suspension of the support material in a non-polar aprotic liquid (NPAL), (b) controlled addition of a Group VIIIB, IB or IIB metal chelate complex with bi- or tri-dentate ligand(s) as a solution in a polar aprotic liquid, (c) filtration, optionally followed by washing with NPAL and (d) optionally removing liquid residues Alternatively, the mixture obtained from stage (b) may be mixed with more NPAL before performing stages (c) and (d) as above. An Independent claim is also included for supported transition metal catalysts obtained by this process.
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公开(公告)号:DE4420642A1
公开(公告)日:1995-12-21
申请号:DE4420642
申请日:1994-06-14
Applicant: BASF AG
Inventor: KRONER MATTHIAS DR , MEYER THOMAS , KLEINKE ANDREAS DR , SCHORNICK GUNNAR DR , MINGES ROLAND DR , LUDWIG ALFONS DR
Abstract: A process is disclosed for preparing polyaspartic acid imides. A mixture of aspartic acid and phosphoric acid in a molar ratio from 1:0.8 to 1:3 is condensed at a temperature from 80 to 150 DEG C into a pre-condensate liquid in the reaction conditions, and the pre-condensate is then polycondensed under shearing at temperatures from 180 to 250 DEG C in a layer with 0.1 to 10 mm thickness.
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公开(公告)号:MY122288A
公开(公告)日:2006-04-29
申请号:MYPI20005088
申请日:2000-10-31
Applicant: BASF AG
Inventor: DEININGER JURGEN , GOTZ WALTER DR , LUDWIG ALFONS DR , PIPPER GUNTER
IPC: C08G69/04 , C08J5/18 , C08G69/00 , C08G69/02 , C08G69/14 , C08G69/16 , C08G69/26 , C08G69/28 , C08G69/36 , C08G69/48 , D01F6/80
Abstract: A PROCESS FOR CONTINUOUS PRODUCTION OF COPOLYAMIDES BASED ON A LACTAM (I), A DIAMINE (II) AND A DICARBOXYLIC ACID (III) COMPRISES REACTING A MIXTURE (IV) COMPRISING A DIAMINE (II), A DICARBOXYLIC ACID (III) AND WATER IN A FIRST REACTION ZONE AT A PRESSURE IN THE RANGE FROM 1.3*105 TO 2.5*105 PA IN THE ENTRY ZONE OF THE REACTION ZONE AND AT A TEMPERATURE ABOVE THE MELTING POINT OF POLYMER (V) TO A CONVERSION, BASED ON THE MOLAR AMOUNTS OF DIAMINE (II) AND DICARBOXYLIC ACID (III), OF AT LEAST 80% TO FORM A POLYMER (V), REACTING A MIXTURE (VI) COMPRISING LACTAM (I) AND WATER IN A SECOND REACTION ZONE AT A PRESSURE IN THE RANGE FROM 5*105 TO 40*105 PA AND AT A TEMPERATURE ABOVE THE MELTING POINT OF POLYMER (VII) TO A CONVERSION, BASED ON THE MOLAR AMOUNT OF LAC TAM (I), OF AT LEAST 80% TO FORM A POLYMER (VII), THEN REACTING POLYMER (V) AND POLYMER (VII) WITH EACH OTHER IN A THIRD REACTION ZONE AT A PRESSURE IN THE RANGE FROM 1*105 TO 1.5*105 PA IN THE ENTRY ZONE OF THE REACTION ZONE AT TEMPERATURES ABOVE THE MELTING POINT OF POLYMER (VIII) TO FORM A POLYMER (VIII), SAID POLYMER (VIII) HAVING A 95°C WATER EXTRACTABLES CONTENT, BASED ON LACTAM (I), DIAMINE (II) AND DICARBOXYLIC ACID (III), OF NOT MORE THAN 10% BY WEIGHT, AND THEN EXTRACTING THE POLYMER (VIII) WITH WATER TO OBTAIN THE COPOLYAMIDE.
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公开(公告)号:DE19752182A1
公开(公告)日:1999-05-27
申请号:DE19752182
申请日:1997-11-25
Applicant: BASF AG
Inventor: HILDENBRAND PETER DR , LANG REINHARD DR , LUDWIG ALFONS DR , PIPPER GUNTER
Abstract: Continuous extraction of polyamide particles with an aqueous extraction medium in an essentially vertical extraction column comprises using subdivided extraction columns in two zones, with extraction in the first zone with 15-40 wt.% aqueous caprolactam and in the second zone with water.
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公开(公告)号:DE19709390A1
公开(公告)日:1998-09-10
申请号:DE19709390
申请日:1997-03-07
Applicant: BASF AG
Inventor: MOHRSCHLADT RALF DR , KRAUS DIETER , LUDWIG ALFONS DR
Abstract: Production of a polyamide from an aminonitrile (AN) and water comprises the combination of steps (1), (2) and (3) or (1), (2), (3) and (4) or (1), (2) and (4) where step (1) involves reacting the AN and water at 100-360 deg C/0.1-35 x 10 Pa; step (2) involves reacting the product of step (1) at 150-400 deg C and a pressure below that in (1) to give a first gas phase and a first liquid and/or solid phase and then separating the phases; step (3) involves reacting the first liquid and/or solid phase with a water-containing gas- or liquid-phase at 150-360 deg C to give a product mixture; and step (4) involves post-condensation of the step (3) product at 200-350 deg C and at a pressure below that in (3) to give a second water- and ammonia-containing gas phase and a second liquid and/or solid phase containing the polyamide. The polyamides prepared using the above combinations of steps are claimed per se. Preferably steps (1) - (4) are effected continuously with recycling of the gas phase obtained in each step to a prior step and with the temperature and pressure in steps (1) and/or (3) such that the gas phase is separated off. Step (1) is such that the conversion of the AN nitrile groups is at least 95 mol.% and a chain extender and/or branching agent may be present. The AN is an 8-13C aminoalkylarylnitrile or an w-aminoalkylnitrile with a 4-12C alkylene group, especially a mixture of (by wt.) 50-99.99% 6-aminocapronitrile; 0.01-50% 4-10C aliphatic- alpha ,w-, 8-12C aromatic- or 5-8C cycloalkane-dicarboxylic acid; 0-50% 4-10C alpha ,w-diamine; 0-50% 2-12C alpha ,w-dinitrile; and 0-50% 5-12C alpha ,w-amino acid or lactam.
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公开(公告)号:DE4430520A1
公开(公告)日:1996-02-29
申请号:DE4430520
申请日:1994-08-27
Applicant: BASF AG
Inventor: KRONER MATTHIAS DR , SCHORNICK GUNNAR DR , STROTMANN UWE DR , SCHWENDEMANN VOLKER DR , LUDWIG ALFONS DR , MEYER THOMAS
Abstract: A process is disclosed for preparing polyaspartic acid salts by treating polycondensates in an aqueous medium with bases. At least 0.7 equivalents of an alkaline metal and/or alkaline earth metal base per mole of the aspartic acid, aspartic acid imide and/or amide units contained in the polycondensates are used. The bases are added during 30 minutes to 20 hours to an aqueous suspension of the polycondensates of aspartic acid heated up to 40 to 140 DEG C, and the reaction mixture is optionally allowed to continue to react. These alkaline metal and/or alkaline earth metal salts of polyaspartic acids obtained by treating aspartic acid polycondensates in an aqueous medium with more than 1 equivalent of an alkaline metal and/or alkaline earth metal base for reducing the molar mass of polycondensates are used as additives for washing and cleaning agents.
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公开(公告)号:DE4428639A1
公开(公告)日:1996-02-15
申请号:DE4428639
申请日:1994-08-12
Applicant: BASF AG
Inventor: KRONER MATTHIAS DR , SCHORNICK GUNNAR DR , FEINDT HANS-JACOB DR , MEYER THOMAS , LUDWIG ALFONS DR , METZMANN UDO
Abstract: Disclosed is a method for producing polyaspartic acid by means of condensation polymerization of finely divided aspartic acid at temperatures above 150 DEG C in the presence of acid catalysts, the acid catalysts being first brought into contact with the finely divided aspartic acid in the reaction zone in which the condensation polymerization takes place.
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