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公开(公告)号:ES2156363T3
公开(公告)日:2001-06-16
申请号:ES97905119
申请日:1997-02-28
Applicant: BASF AG
Inventor: BAUR KARL GERHARD , FISCHER ROLF , PINKOS ROLF , STEIN FRANK , RUST HARALD , BREITSCHEIDEL BORIS
IPC: B01J23/80 , B01J23/889 , C07B61/00 , C07C29/149 , C07C31/20
Abstract: PCT No. PCT/EP97/00980 Sec. 371 Date Aug. 28, 1998 Sec. 102(e) Date Aug. 28, 1998 PCT Filed Feb. 28, 1997 PCT Pub. No. WO97/31882 PCT Pub. Date Sep. 4, 19971,6-Hexanediol is prepared from a carboxylic acid mixture comprising adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols which is obtained as a by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol by water extraction of the reaction mixture, by esterification of the acids and hydrogenation wherein a) the monocarboxylic and dicarboxylic acids present in the aqueous dicarboxylic acid mixture are reacted with a low molecular weight alcohol to give the corresponding carboxylic esters, b) the resulting esterification mixture is freed of excess alcohol and low boilers in a first distillation stage, c) the bottoms are fractionated in a second distillation stage to give an ester fraction essentially free of 1,4-cyclohexanediols and a fraction comprising at least the major part of the 1,4-cyclohexanediols, d) the ester fraction essentially free of 1,4-cyclohexanediols is catalytically hydrogenated and e) in a pure distillation stage, 1,6-hexanediol is isolated from the hydrogenation product in a manner known per se.
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公开(公告)号:DE59703470D1
公开(公告)日:2001-06-07
申请号:DE59703470
申请日:1997-02-28
Applicant: BASF AG
Inventor: BAUR GERHARD , FISCHER ROLF , PINKOS ROLF , STEIN FRANK , RUST HARALD , BREITSCHEIDEL BORIS
IPC: B01J23/80 , B01J23/889 , C07B61/00 , C07C29/149 , C07C31/20
Abstract: PCT No. PCT/EP97/00980 Sec. 371 Date Aug. 28, 1998 Sec. 102(e) Date Aug. 28, 1998 PCT Filed Feb. 28, 1997 PCT Pub. No. WO97/31882 PCT Pub. Date Sep. 4, 19971,6-Hexanediol is prepared from a carboxylic acid mixture comprising adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols which is obtained as a by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol by water extraction of the reaction mixture, by esterification of the acids and hydrogenation wherein a) the monocarboxylic and dicarboxylic acids present in the aqueous dicarboxylic acid mixture are reacted with a low molecular weight alcohol to give the corresponding carboxylic esters, b) the resulting esterification mixture is freed of excess alcohol and low boilers in a first distillation stage, c) the bottoms are fractionated in a second distillation stage to give an ester fraction essentially free of 1,4-cyclohexanediols and a fraction comprising at least the major part of the 1,4-cyclohexanediols, d) the ester fraction essentially free of 1,4-cyclohexanediols is catalytically hydrogenated and e) in a pure distillation stage, 1,6-hexanediol is isolated from the hydrogenation product in a manner known per se.
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公开(公告)号:ID27962A
公开(公告)日:2001-05-03
申请号:ID20010646
申请日:1999-09-16
Applicant: BASF AG
Inventor: FISCHER ROLF , LIANG SHELUE , PINKOS ROLF
IPC: C07D307/08
Abstract: In a process for preparing THF (tetrahydrofuran) by reaction of a 1,4-butanediol-containing reaction mixture over an acid catalyst, the reaction mixture comprises further alcohols different from 1,4-butanediol and is essentially free of water.
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公开(公告)号:GR3033955T3
公开(公告)日:2000-11-30
申请号:GR20000401640
申请日:2000-07-14
Applicant: BASF AG
Inventor: BAUR KARL GERHARD , FISCHER ROLF , PINKOS ROLF , STEIN FRANK , BREITSCHEIDEL BORIS , RUST HARALD
IPC: C07D313/04 , C07C27/12 , C07C29/149 , C07C29/80 , C07C29/88 , C07C31/20 , C07C31/27 , C07C51/31 , C07D315/00
Abstract: PCT No. PCT/EP97/00990 Sec. 371 Date Aug. 28, 1998 Sec. 102(e) Date Aug. 28, 1998 PCT Filed Feb. 28, 1997 PCT Pub. No. WO97/31883 PCT Pub. Date Sep. 4, 19971,6-hexanediol and epsilon -caprolactone are prepared from a carboxylic acid mixture comprising adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols which is obtained as a by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol using oxygen or oxygen-containing gases by water extraction of the reaction mixture, by esterifying and hydrogenating a substream to give hexanediol and cyclizing 6-hydroxycaproic esters to give caprolactone.
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公开(公告)号:DK0883591T3
公开(公告)日:2000-08-07
申请号:DK97905123
申请日:1997-02-28
Applicant: BASF AG
Inventor: BAUR KARL GERHARD , FISCHER ROLF , PINKOS ROLF , STEIN FRANK , BREITSCHEIDEL BORIS , RUST HARALD
IPC: C07C29/149 , C07C31/20 , C07D313/04
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公开(公告)号:ES2139348T3
公开(公告)日:2000-02-01
申请号:ES96910004
申请日:1996-03-21
Applicant: BASF AG
Inventor: FISCHER ROLF , PINKOS ROLF
IPC: B01J23/46 , B01J23/656 , B01J23/755 , B01J23/889 , B01J23/89 , C07B61/00 , C07C29/10 , C07C29/132 , C07C29/141 , C07C29/17 , C07C31/20 , C07D307/08
Abstract: PCT No. PCT/EP96/01247 Sec. 371 Date Sep. 16, 1997 Sec. 102(e) Date Sep. 16, 1997 PCT Filed Mar. 21, 1996 PCT Pub. No. WO96/29322 PCT Pub. Date Sep. 26, 19961,4-butanediol and THF are prepared from furan by a process which comprises converting furan in the presence of water and hydrogen but in the absence of a water-soluble acid in a single stage over a hydrogenation catalyst, the hydrogenation catalyst containing at least one element of subgroup I, V, VI, VII or VIII in the form of a compound or in elemental form and the restriction that the catalyst does not contain nickel alone being applicable.
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公开(公告)号:CA2329477A1
公开(公告)日:1999-11-04
申请号:CA2329477
申请日:1999-04-16
Applicant: BASF AG
Inventor: FISCHER ROLF , KAIBEL GERD , PINKOS ROLF , RAHN RALF-THOMAS
IPC: C07C29/149 , C07C29/17 , C07C31/20 , C07C51/16 , C07C67/03 , C07C67/08 , C07C69/60 , C07D307/08 , C07D307/32 , C07D307/33 , C07D315/00
Abstract: The invention relates to a method for producing 1,4-butanediol and possibly .gamma.-butyrolactone and tetrahydrofurane by oxidation of butane or benzol into a product flow containing maleic anhydride, absorption of maleic anhydride from the product flow by means of an inert, high-boiling solvent in an absorption stage, which yields a liquid absorption product, and esterification of said liquid absorption product with a C1-C5 esterification alcohol in an esterification step, yielding an esterification product containing the corresponding diester and high-boiling inert solvent. This is followed by hydrogenation of the esterification product, which results in an hydrogenation product containing the products 1,4-butanediol and optionally .gamma.-butyrolactone and tetrahydrofurane as well as the esterification alcohol. The hydrogenation product is separated by distillation into the products and the esterification alcohol and the esterification alcohol is returned to the esterification zone. Prior to hydrogenation the esterification product is separated by distillation under reduced pressured into the diester and the inert solvent, the inert solvent is returned to the absorption stage and the diester is hydrogenated in the liquid phase on a fixed-bed catalyst.
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公开(公告)号:RU2135456C1
公开(公告)日:1999-08-27
申请号:RU96116892
申请日:1995-01-12
Applicant: BASF AG
Inventor: KANAND JUERGEN , ROEPER MICHAEL , PINKOS ROLF , ROKKO PACHELLO , THOME ALFRED
IPC: B01J21/16 , B01J27/18 , B01J29/06 , C07B61/00 , C07C27/00 , C07C29/17 , C07C31/12 , C07C41/06 , C07C41/32 , C07C43/15 , C07C45/51 , C07C47/02
Abstract: FIELD: industrial organic synthesis. SUBSTANCE: 1,3-butadiene interacts with alcohol of formula ROH, wherein R is alkyl or alkenyl with 2-20 carbon atoms optionally substituted by one or two C 1 -C 10 -alkoxy or hydroxy-C 1 -C 10 -alkoxy groups; C 6 -C 10 -aryl; C 7 -C 11 -arylalkyl; or methyl at elevated temperatures and pressure in presence of Broensted acid or Ib, VIIb or VIIIb group element complex with phosphorus- or nitrogen-containing ligands to form adducts corresponding to structures C-C=C-C-OR (II) and C-C(OR)-C=C (III). Adduct III is isomerized into adduct II. The latter is subjected to isomerization in presence of transition metal-containing homogeneous or heterogeneous catalyst in liquid phase or in presence of transition metal-containing heterogeneous catalyst in gas phase to form enol ether with structure C-C- C=C-OR (IV). Enol ether IV is subjected to action of hydrogen and water or only water in presence of homogeneous or heterogeneous catalyst as indicated above to form n-butyraldehyde and/or n-butanol, from which alcohol ROH is further released and recycled into the first step of process. EFFECT: increased selectivity of process and yield of products. 7 cl, 1 dwg, 6 tbl, 15 ex
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公开(公告)号:ES2130780T3
公开(公告)日:1999-07-01
申请号:ES96900564
申请日:1996-01-04
Applicant: BASF AG
Inventor: DOSTALEK ROMAN , FISCHER ROLF , HARDER WOLFGANG , PAUL AXEL , PINKOS ROLF
Abstract: PCT No. PCT/EP96/00023 Sec. 371 Date Jul. 1, 1997 Sec. 102(e) Date Jul. 1, 1997 PCT Filed Jan. 4, 1996 PCT Pub. No. WO96/20909 PCT Pub. Date Jul. 11, 1996Impurities are separated from aqueous solutions of 1,6-hexanediol or 1,6-hexanediol precursors, such as adipic and 6-hydroxycaproic acid, by a process which comprises adding at least one carboxylic acid to a solution (a) of 1,6-hexanediol and subjecting this solution (a) or a solution (b) containing carboxylic acid(s) as precursor(s) of 1,6-hexanediol to a heat treatment at temperatures above room temperature in the absence of hydrogen.
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110.
公开(公告)号:CA2303372A1
公开(公告)日:1999-03-18
申请号:CA2303372
申请日:1998-08-27
Applicant: BASF AG
Inventor: PINKOS ROLF , STEIN FRANK , LIANG SHELUE , FISCHER ROLF HARTMUTH
IPC: B01J21/04 , B01J21/06 , B01J23/06 , B01J23/10 , C07B61/00 , C07C45/54 , C07C49/395 , C07C51/377 , C07C61/20 , C07C67/317 , C07C67/333 , C07C69/74
Abstract: The invention relates to a method for producing cyclopentanone and cyclopentene-1-carboxylic acid or their esters of formula (I) COOR, wherein R represents hydrogen or an aliphatic radical with 1 to 6 C-atoms or a cycloaliphatic, araliphatic or aromatic radical with 6 to 12 C-atoms. According to said method, compounds of formula (II) X-(CH2)4-COOR, wherein X represents a formyl- or hydroxymethyl radical and R has the meaning given above, and/or compounds which can be converted into compounds of formula (II) with water or alcohols ROH under the reaction conditions are heated in the gaseous or liquid phase to temperatures of 200 to 450 ~C in the presence of heterogeneous oxidic catalysts.
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