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公开(公告)号:DE2949073A1
公开(公告)日:1981-06-11
申请号:DE2949073
申请日:1979-12-06
Applicant: BASF AG
Inventor: KUMMER RUDOLF DIPL CHEM DR , TAGLIEBER VOLKER DIPL CHEM DR , WEISS FRANZ-JOSEF DIPL CHEM DR , SCHNEIDER HEINZ-WALTER DIPL CH
Abstract: A process for purifying carboxylic acid esters which have been obtained by reacting olefinically unsaturated compounds with carbon monoxide and alkanols and which contain aldehydes or acetals, wherein the said esters are treated with a strongly acidic agent, with or without addition of water.
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公开(公告)号:DE2924785A1
公开(公告)日:1981-01-29
申请号:DE2924785
申请日:1979-06-20
Applicant: BASF AG
Inventor: KUMMER RUDOLF DIPL CHEM DR , SCHNEIDER HEINZ-WALTER DIPL CH , TAGLIEBER VOLKER DIPL CHEM DR , WEISS FRANZ-JOSEF DIPL CHEM DR
IPC: C07C67/08 , B01J31/00 , B01J31/20 , C07B61/00 , C07C67/38 , C07C67/58 , C07C69/34 , C07C69/44 , C07C69/533
Abstract: A process for the preparation of butanedicarboxylic acid esters, wherein (a) an aqueous cobalt salt solution is treated with excess carbon monoxide and hydrogen in the presence of active charcoal laden with cobalt carbonyl, (b) the resulting aqueous solution of cobalt carbonyl hydride is extracted with butadiene or a butadiene containing hydrocarbon mixture and the aqueous phase is separated off, (c) the butadiene, or butadiene/hydrocarbon mixture, containing cobalt carbonyl hydride, cobalt carbonyl and butenyl-cobalt tricarbonyl, is reacted with carbon monoxide and excess C1-C4-alkanol in the presence of a tertiary nitrogen base, (d) the resulting reaction mixture is freed from the tertiary nitrogen base contained therein, down to a content of from 0.1 to 0.3 mole per mole of pentenoic acid ester, and from excess hydrocarbons, and the pentenoic acid ester remaining in the reaction mixture is reacted with carbon monoxide and excess C1-C4-alkanol in the presence of the cobalt carbonyl and tertiary nitrogen base contained in the reaction mixture, (e) the reaction mixture is treated with an oxidizing agent in the presence of the aqueous acid solution which has been separated off in stage (b), and the mixture is separated into an organic phase, from which butanedicarboxylic acid esters are isolated by distillation, and an aqueous phase, and (f) the aqueous phase is extracted with water-immiscible solvents, the phases are separated, and the resulting aqueous phase is freed from alkanols and tertiary nitrogen base and is recycled to stage (a).
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公开(公告)号:DE2630086A1
公开(公告)日:1978-01-12
申请号:DE2630086
申请日:1976-07-03
Applicant: BASF AG
Inventor: PLATZ ROLF DIPL CHEM DR , KUMMER RUDOLF DIPL CHEM DR , SCHNEIDER HEINZ-WALTER DIPL CH , SCHWIRTEN KURT DIPL CHEM DR
IPC: C07C69/533 , B01J31/00 , C07B61/00 , C07C51/00 , C07C51/14 , C07C57/03 , C07C67/00 , C07C69/52 , C07C57/02 , C07C67/38
Abstract: A process for the manufacture of pent-3-enoic acid and its alkyl esters, of the general formula CH3-CH=CH-CH2-CO-OR where R is hydrogen or alkyl of 1 to 4 carbon atoms, comprising carbonylating butadiene with carbon monoxide and a compound ROH at from 300 to 1,000 bars CO pressure and from 100 DEG to 160 DEG C. in the presence of cobalt catalysts and nitrogen bases, wherein C4 cuts are used as starting materials and a tertiary amine having a pKA of from 3 to 11 is used as the nitrogen base. The pent-3-enoic acid or alkyl esters produced may be used for the manufacture of adipic acid or its alkyl esters, which compounds are starting materials for the manufacture of nylons.
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公开(公告)号:DE2332638A1
公开(公告)日:1975-01-23
申请号:DE2332638
申请日:1973-06-27
Applicant: BASF AG
Inventor: STROHMEYER MAX DIPL CHEM DR , NIENBURG HANS JUERGEN DR , KUMMER RUDOLF DIPL CHEM DR , HOHENSCHUTZ HEINZ DIPL CHEM DR
Abstract: Solutions of cobalt carbonyl and cobalt carbonyl hydride in organic solvents are prepared by treating aqueous solutions of cobalt salts with carbon monoxide and hydrogen at a temperature of from 50 DEG to 200 DEG C and a pressure of from 50 to 500 atmospheres in the presence of solvents which are sparingly water-miscible or are water-immiscible and which have a content of cobalt carbonyl, cobalt carbonyl hydride or mixtures thereof, the starting materials and the organic solvents being passed cocurrently through a zone in which a turbulent flow is maintained. The improvement includes using n-butanol as solvent. Solutions of cobalt carbonyl and cobalt carbonyl hydride in n-butanol are suitable as catalyst solutions for oxo syntheses.
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公开(公告)号:DE3220858A1
公开(公告)日:1983-12-08
申请号:DE3220858
申请日:1982-06-03
Applicant: BASF AG
Inventor: ELLIEHAUSEN HEINRICH DIPL CHEM , FISCHER KARL DIPL CHEM DR , HERR MANFRED DIPL ING , STROHMEYER MAX DIPL CHEM DR , KUMMER RUDOLF DIPL CHEM DR , ROMBERG HELMUT DIPL ING DR , SCHWIRTEN KURT DIPL CHEM DR , RICHTER WOLFGANG DIPL CHEM DR
Abstract: Hydroformylation of olefinically unsaturated compounds by means of triorganorhodium (rhodium/triorganyl) complexes at 80 to 140 DEG C and 10 to 40 bar by using for this purpose a cylindrical reactor (1) - see figure - equipped with an axially arranged nozzle (2) for introduction of the olefinic compound and the synthesis gas consisting of H2 and CO, a valve (3) for discharging the material and a concentric tube (4) whose height is about 20 to 70 % of the reactor height and whose diameter is about 30 to 80 % of the reactor diameter and which is arranged above the nozzle (2) at a distance of about 1 to 3 times its diameter, the momentum of the gases entering through (2) being such that the mean linear flow rate of the liquid reactor contents is 0.1 to 1.0 m/sec.
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公开(公告)号:DE2836518A1
公开(公告)日:1980-03-06
申请号:DE2836518
申请日:1978-08-21
Applicant: BASF AG
IPC: B01J31/00 , C07B61/00 , C07C67/38 , C07C69/44 , C07C69/533
Abstract: Multistep process for the preparation of butanedicarboxylic acid by the hydrogenation of carbon monoxide under pressure in the presence of a cobalt carbonyl catalyst, the improvement of heating at a temperature of 250 DEG to 350 DEG C. under superatmospheric pressure the resulting aqueous solution of cobalt carbonyl hydride that has been extracted with butadiene or with mixtures thereof before using in a subsequent step of the multistep process.
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公开(公告)号:DE2638824A1
公开(公告)日:1978-03-02
申请号:DE2638824
申请日:1976-08-28
Applicant: BASF AG
IPC: C07C55/02 , C07C51/00 , C07C55/10 , C07C55/12 , C07C55/14 , C07C55/16 , C07C55/18 , C07C55/20 , C07C55/21 , C07C67/00 , C07C209/00 , C07C211/09 , C07C87/14
Abstract: A process for the manufacture of salts of alkanedicarboxylic acids of 4 to 12 carbon atoms and alkanediamines of 3 to 14 carbon atoms, comprising reacting esters of alkanols of 1 to 4 carbon atoms and alkanedicarboxylic acids of 4 to 12 carbon atoms with alkanediamines of 3 to 14 carbon atoms in stoichiometric amounts in the presence of water at an elevated temperature, with continuous removal of the alkanols formed, in which process the reaction is carried out, from the start, in the presence of the particular salt of alkanedicarboxylic acid and alkanediamine which is to be manufactured.
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公开(公告)号:DE2604545A1
公开(公告)日:1977-08-18
申请号:DE2604545
申请日:1976-02-06
Applicant: BASF AG
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19.
公开(公告)号:DE2537448A1
公开(公告)日:1977-03-03
申请号:DE2537448
申请日:1975-08-22
Applicant: BASF AG
IPC: C07C45/49 , C07C47/198 , C07C47/02 , C07C43/30 , C07C45/10
Abstract: Acetals of hexan-1-al substd. in the 6-position having formula (R-O)-2CH-(CH2)4-A, where R = Me, Et or both gps. form a 1,2 or 1,3-alkylene group with 2-4C; A = formyl, hydroxymethyl, aminomethyl. Cpds. (I) can be used in the prepn. of caprolactam, hexamethylene diamine and hexan-1,6-diol; also e.g. in the prepn. of crosslinked polyurethanes.
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公开(公告)号:DE2451473A1
公开(公告)日:1976-05-13
申请号:DE2451473
申请日:1974-10-30
Applicant: BASF AG
Inventor: KUMMER RUDOLF DIPL CHEM DR
Abstract: Prepn. of formyl propyl acetates of formula OHC -(n-C3H6)-O-CO-CH3 (I) (where formyl gp. can be in position 1, 2 or 3 of n-C H6 grouping) by hydroformylation of allyl acetate with CO and H2 in the presence of an organic solvent and CO2(CO)8 as catalyst takes place by (a) using paraffins or paraffin mixts. which are liquid at 40-120 degrees C as organic solvents, and (b) maintaining in paraffin phase a concn. of 0.05-1.5 wt. % CO2(CO)8, w.r.t. paraffin. (I) can be obtd. in >95% purity and 85-95% yields; reaction times are short and reaction mixt. is easily processed; (I) are insoluble in paraffins whereas CO2(CO)8 can be enriched therein to an extent of 70-80%. Catalyst-contg. paraffin phase can be returned to hydroformylation after separating (I). Isomer mixt. (I) can be hydrogenated to diols, useful as components in polyester and polyurethane chemistry.
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