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公开(公告)号:DE19647349A1
公开(公告)日:1998-05-20
申请号:DE19647349
申请日:1996-11-15
Applicant: BASF AG
Inventor: BAUR KARL GERHARD DR , FISCHER ROLF DR , PINKOS ROLF DR , STEIN FRANK DR , RUST HARALD , BREITSCHEIDEL BODO DR
IPC: C07C29/149 , C07D315/00 , C07C31/20 , C07C29/136 , C07C29/74 , C07C29/80 , C07C29/88 , C07C69/48 , C07C69/675 , C07D313/04
Abstract: Preparation of 2,6-hexandiol and iota -caprolactone from a carboxylic acid mixture containing adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexandiols. The mixture is obtained as a by-product of the oxidation of cyclohexane into cyclohexanone and cyclohexanol with oxygen or oxygen-containing gases, water extraction, esterification and hydrogenation into hexandiol and cyclisation of 6-hydroxycaproic acid esters into caprolactone. Steps involved are: (a) esterification of the monocarboxylic and dicarboxylic acids in the aqueous reaction mixture with low molecular mass alcohols, (b) excess alcohol and low b.pt. substances are distilled off, (c) a second distillation step separates the mixture into an ester fraction substantially free of 1,4-cyclohexandiols and one containing at least the greater part of the 1,4-cyclohexandiols, (d) at least part of a substantially 6-hydroxycaproic acid ester stream is separated from the ester fraction in a third distillation stage, (e) the ester fraction from (d) from which the 6-hydroxycaproic acid ester was at least partially removed, is hydrogenated catalytically and 1,6-hexandiol is extracted by distillation and (f) the substantially 6-hydroxycaproic acid ester containing stream is heated above 200 deg C at reduced pressure so as to effect cyclisation. Pure iota -caprolactone is recovered by distillation. Preferably water is removed from the carboxylic acid mixture before esterification. Alcohol for esterification is either 1-3C (preferably MeOH) or 4-10C (preferably iso-BuOH or tert.-BuOH) and a variety of distillation, collection and separation arrangements are used depending on the relative b.pts. of the intermediate products involved. A Cu, Co and/or Re based catalyst is used for the hydrogenation step, or one of type CuaAlbZrcMndOx (a > 0, b > 0, c \- 0, d > 0, a > b/2, b > a/4, a > c, a > d and x = a number to balance the formula).
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公开(公告)号:MY137707A
公开(公告)日:2009-02-27
申请号:MYPI20015608
申请日:2001-12-10
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH DR , WECK ALEXANDER , STEIN FRANK DR , PINKOS ROLF DR , HESSE MICHAEL DR , SPRAGUE MICHAEL JOLYON DR , SCH MARKUS R XD DR , BORCHERT HOLGER DR , SCHLITTER STEPHAN DR , RAHN RALF-THOMAS DR
IPC: B01J23/72 , B01J23/80 , C07C27/06 , C07D307/08
Abstract: UNSUBSTITUTED OR ALKYL-SUBSTITUTED THF IS OBTAINED BY CATALYTIC HYDROGENATION IN THE GAS PHASE OF C4-DICARBOXYLIC ACIDS AND/OR THEIR DERIVATIVES USING A CATALYST COMPRISING 20BY WEIGHT, PREFERABLY >30BY WEIGHT IN PARTICULARLY FROM 35 TO 90BY WEIGHT, OF AN OXIDIC SUPPORT HAVING ACID CENTERS, AT A HOT SPOT TEMPERATURE OF FROM 240 TO 310°C, PREFERABLY FROM 240 TO 280°C, AND A WHSV OVER THE CATALYST OF FROM 0.01 TO 1.0, PREFERABLY FROM0.02 TO 1, IN PARTICULARLY FROM 0.05 TO 0.5, kg OF STARTING MATERIAL/L OF CATALYST x HOUR.
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公开(公告)号:DE19756171A1
公开(公告)日:1999-07-01
申请号:DE19756171
申请日:1997-12-17
Applicant: BASF AG
Inventor: DOSTALEK ROMAN DR , FISCHER ROLF DR , KRUG THOMAS , PAUL AXEL DR , PINKOS ROLF DR , STEIN FRANK DR
Abstract: The invention relates to a method for catalytically hydrogenating carboxylic acids or the anhydrides or esters thereof into alcohol on heterogeneous catalysts containing hydrogenating elements of groups 6, 7, 8, 9, 10 and 11 and optionally groups 2, 14 and 15 of the periodic table of elements or consisting thereof, in a liquid phase at temperatures of 100-300 DEG C and at pressures of 10-300 bars, whereby 1-3,000 ppm of a basic alkali or earth-alkaline compound in relation to the liquid hydrogenating feed and selected from a group consisting of hydroxides, carbonates, carboxylates and alcoholates is added to the hydrogenating reaction mixture.
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公开(公告)号:DE19757554A1
公开(公告)日:1999-06-24
申请号:DE19757554
申请日:1997-12-23
Applicant: BASF AG
Inventor: LIANG SHELUE DR , FISCHER ROLF HARTMUTH DR , PINKOS ROLF DR , STEIN FRANK DR , BREITSCHEIDEL BORIS DR
IPC: C07B61/00 , C07C29/149 , C07C31/20
Abstract: 1,6-Hexanediol is produced by gas-phase hydrogenation of adipate and/or 6-hydroxycaproate esters at 150-230 deg C and 10-70 bar on chromium-free catalysts essentially containing copper, manganese and aluminium or on Raney copper, with a hydrogen:ester mol ratio of (150:1) - (300:1) and a catalyst loading of 0.01-0.3 kg 6C-ester/l catalyst/hour.
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5.
公开(公告)号:DE19647348A1
公开(公告)日:1998-05-20
申请号:DE19647348
申请日:1996-11-15
Applicant: BASF AG
Inventor: BAUR KARL GERHARD DR , FISCHER ROLF DR , PINKOS ROLF DR , STEIN FRANK DR , RUST HARALD , BREITSCHEIDEL BODO DR
IPC: C07C29/149 , C07C31/20 , C07C29/136 , C07C29/74 , C07C29/80 , C07C29/88
Abstract: A process for the production of 1,6-hexandiol (I) from a carboxylic acid mixture (II) of adipic acid, 6-hydroxycaproic acid and small amounts of cyclohexan-1,4-diol(s) is obtained as by-product of the oxidation of cyclohexane to cyclohexanone/cyclohexanol with (gas containing) oxygen by extraction of the reaction mixture with water. The process involves esterification of the acids and hydrogenation. First, (a) the mono- and dicarboxylic acids in the aqueous (II) are esterified with a low molecular alcohol. This is followed by 2 distillation stages, in which (b) excess alcohol and low-boiling compounds are removed and (c) the sump is separated into an ester fraction free from cyclohexan-1,4-diol(s) and a fraction of (mainly) cyclohexan-1,4-diol(s). Then (d) the ester fraction is hydrogenated catalytically and (e) pure (I) is recovered from the hydrogenation product by distillation.
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公开(公告)号:DE19739441A1
公开(公告)日:1999-03-11
申请号:DE19739441
申请日:1997-09-09
Applicant: BASF AG
Inventor: FISCHER ROLF DR , LIANG SHELUE DR , PINKOS ROLF DR , STEIN FRANK DR
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 , C07C51/347 , C07C45/48 , C07D223/10
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 DEG C in the presence of heterogeneous oxidic catalysts.
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公开(公告)号:DE19719875A1
公开(公告)日:1998-11-19
申请号:DE19719875
申请日:1997-05-12
Applicant: BASF AG
Inventor: ELLER KARSTEN DR , STEIN FRANK DR , SIGWART CHRISTOPH DR , BECKER RAINER DR , PLITZKO KLAUS-DIETER DR , FISCHER ROLF DR , MUELLER ULRICH DR
Abstract: The invention relates to a method for polymerizing cyclic ether on a heterogeneous catalyst, wherein the heterogeneous catalyst contains one or several pillared interlayered clays (PILCs).
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公开(公告)号:DE19648244A1
公开(公告)日:1998-05-28
申请号:DE19648244
申请日:1996-11-21
Applicant: BASF AG
Inventor: STEIN FRANK DR , LIANG SHELUE DR , FISCHER ROLF DR , PINKOS ROLF DR , BREITSCHEIDEL BORIS DR
IPC: C07D315/00 , C07D309/30 , C07B41/12 , C07B43/06 , C07C275/64 , C07D313/04 , C07H1/00 , C07K1/10
Abstract: Method for producing delta - and epsilon -lactones of formula (I), in which the radical R may be the same or different, and stand for hydrogen, optionally substituted aliphatic, cycloaliphatic, aromatic, araliphatic or heterocyclic radicals, which can also be optionally bond to an oxygen atom of C atom and n stands for the numbers 3 or 4. According to said method, dialdehyde of the formula (II) OCH- (CR2)n-CHO, wherein R and n have the meaning cited above, or the mono- and the dihydrates and/or the mono- and the dihemiacetales of said dialdehydes are made to react in heterogeneous catalyzers during the gas or liquid phase at temperatures ranging from 20 to 300 DEG C and pressures ranging from 0.1 to 100 bar and the lactones are obtained in pure form by distillation.
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公开(公告)号:DE19641481A1
公开(公告)日:1998-04-16
申请号:DE19641481
申请日:1996-10-09
Applicant: BASF AG
Inventor: SIGWART CHRISTOPH DR , ELLER KARSTEN DR , BECKER RAINER DR , PLITZKO KLAUS-DIETER DR , FISCHER ROLF HARTMUTH DR , STEIN FRANK DR , MUELLER ULRICH DR , HESSE MICHAEL DR
Abstract: The invention concerns a process for preparing polytetrahydrofuran, copolymers of tetrahydrofuran and 2-butin-1,4-diol, diesters of these polymers with C2-C20 monocarboxylic acids or monoesters of these polymers with C1-C10 monocarboxylic acids by polymerizing tetrahydrofuran in the presence of one of the following telogens, water, 1,-4-butane diol, 2-butin-1,4-diol, polytetrahydrofuran with a molecular weight of between 200 and 700 Dalton, or of a C1-C10 monocarboxylic acid or a carboxylic acid anhydride produced from C2-C20 monocarboxylic acids or mixtures of these telogens on a heterogeneous carrier catalyst which contains a catalytically active amount of an oxygenous molybdenum and/or tungsten compound on an oxidic carrier material, and which has been calcined at temperatures of between 500 DEG C and 1000 DEG C after application of the precursor compounds of the oxygenous molybdenum and/or tungsten compounds to the carrier material precursors. Before it is used as a polymerization catalyst, the catalyst is activated by treatment with a reducing agent.
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10.
公开(公告)号:MY136889A
公开(公告)日:2008-11-28
申请号:MYPI20015864
申请日:2001-12-24
Applicant: BASF AG
Inventor: GALL MARTIN , KAIBEL GERD DR , KRUG THOMAS , RUST HARALD , STEIN FRANK DR
IPC: C07D309/30 , B01D3/14 , C07C29/80 , C07C31/20 , C07D315/00
Abstract: A PROCESS FOR WORKING UP BY DISTILLATION THE CRUDE PRODUCTS OBTAINED IN THE PROCESS ACCORDING TO DE-A 196 07 954 AND CONTAINING 1,6-HEXANIDIOL (HDO),1,5-PENTANIDIOL (PDO) OR CAPROLACTONE (CLO) IN ORDER IN OBTAIN THE CORESPONDING PURE PRODUCTS,THE WORKING-UP BY DISTILLATION BEONG CARIED OUT IN EACH CASE IN A DIVIDING WALL COLUMN (TK) IN WHICH A DIVIDING WALL (T) IS ARRANGED IN THE LOGITUDINAL DIRECTION OF DIRECTION OF THE COLUMN WITH FORMATION OF AN UPPER COMMON COLUMN REGION (1),A LOWER COMMON COLUMN REGION (6),A FEED SECTION (2,4) HAVING A RECTIFICATION SECTION (2) AND STRIPPING SECTION (4) AND A TAKE-OFF SECTION (3,5) HAVING A STRIPPING SECTION (3) AND RETIFICATION SECTION (5),WITH FEEDING OF THE RESPECTIVE CRUDE PRODUCT HDO,PLO OR CLO IN THE MIDDLE REGION OF THE FEED SECTION (2,4) AND REMOVAL OF THE HIGH BOILER FRACTION (C) FROM THE BOTTOM OF THE COLUMN,OF THE LOW BOILER FRACTION (A) VIA THE TOP OF COLUMN AND OF THE MEDIUM BOILRE FRACTION (B) FROM THR MIDDLE REGION OF THE TAKE-OFF SECTION (3,5),OR IN THERMALLY COUPLED COLUMNS.
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