21.
    发明专利
    未知

    公开(公告)号:DE50005700D1

    公开(公告)日:2004-04-22

    申请号:DE50005700

    申请日:2000-06-21

    Applicant: BASF AG

    Abstract: A process for preparing 1,6-hexanediol from a carboxylic acid mixture comprising adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols which is obtained as by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol after water extraction of the reaction mixture followed by extraction with aqueous sodium hydroxide solution, by esterification of the acids and hydrogenation comprisesa) liberating the carboxylic acids from the alkaline extract by addition of a mineral acid,b) fractionating the organic phase comprising carboxylic acids to give a distillate comprising the low molecular weight monocarboxylic acids and a residue comprising adipic acid and 6-hydroxycaproic acid,c) reacting the monocarboxylic an dicarboxylic acids present in the aqueous dicarboxylic acid mixture with a low molecular weight alcohol to give the corresponding carboxylic esters,d) freeing the esterification mixture obtained of excess alcohol and low boilers in a first distillation step,e) fractionating the bottom product in a second distillation step 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,f) catalytically hydrogenating the ester fraction which is essentially free of 1,4-cyclohexanediols andg) isolating 1,6-hexanediol from the hydrogenation product in a manner known per se in a final distillation step.

    PREPARATION OF 1, 6-HEXANEDIOL AND 6-HYDROXYCAPROIC ACID AND ESTERS THEREOF

    公开(公告)号:MY116778A

    公开(公告)日:2004-03-31

    申请号:MYPI9804995

    申请日:1998-11-03

    Applicant: BASF AG

    Abstract: A PROCESS FOR THE PREPARATION OF L, 6-HEXANEDIOL AND 6-HYDROXYCAPROIC ACID OR ESTERS THEREOF BY CATALYTIC HYDROGENATION OF ADIPIC ACID, ADIPIC ACID MONOESTERS OR ADIPIC ACID DIESTERS OR STREAMS OF STARTING MATERIAL WHICH CONTAIN ADIPIC ACID OR ESTERS THEREOF AS ESSENTIAL CONSTITUENTS, IN WHICH THE BOTTOM PRODUCT OBTAINED IN THE DISTILLATION OF THE HYDROGENATION PRODUCT, FOLLOWING REMOVAL OF THE HEXANEDIOL AND HYDROXYCAPROIC ACID OR ESTERS THEREOF, AND ESSENTIALLY COMPRISES OLIGOMERIC ESTERS OF 6-HYDROXYCAPROIC ACID, IS RECYCLED TO THE HYDROGENATION, AND THE RESULTING ''MIXTURE OF STARTING MATERIAL AND RECYCLE STREAM IS REACTED AT FROM 100 TO 300°C, AT FROM 10 TO 300 BAR IN THE LIQUID PHASE AND AT A MOLAR RATIO OF CARBOXYL GROUPS TO BE HYDROGENATED TO HYDROGEN IN THE REACTOR OF FROM 1 : 5 TO 1 : 100 ON HYDROGENATION CATALYSTS IS DESCRIBED.

    METHOD AND DEVICE FOR THE DISTILLATIVE PROCESSING OF 1,6-HEXANDIOL, 1,5-PENTANDIOL AND CAPROLACTONE

    公开(公告)号:CA2433073A1

    公开(公告)日:2002-07-18

    申请号:CA2433073

    申请日:2002-01-08

    Applicant: BASF AG

    Abstract: The invention relates to a method for the distillative processing of the crude products 1,6-hexandiols (HDO), 1,5-pentandiol (PDO) or caprolactone (CLO) obtained according to the method of German patent application DE-A 196 07 954 in order to obtain the corresponding pure products. The distillative processing proceeds in a separation column (TK) in which a separating wall (T) is arranged in the column longitudinal direction forming an upper common column section (1), a lower common column section (6), a feed part (2, 4) with reinforcement part (2) and drive part (4), and a removal part (3, 5) with output part (3) and reinforcement part (5). The corresponding crude product HDO, PDO or CLO is fed in the center section of the feed part (2, 4), the high- boiling fraction (C) is removed from the column sump, the low-boiling fraction (A) is removed via the column head and the medium-boiling fraction (B) is removed from the center section of the removal part (3, 5). The inventive method can also be carried out in thermally coupled columns.

    24.
    发明专利
    未知

    公开(公告)号:AT192730T

    公开(公告)日:2000-05-15

    申请号:AT97905123

    申请日:1997-02-28

    Applicant: BASF AG

    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.

    METHOD FOR PRODUCING HEXANEDIOL
    25.
    发明专利

    公开(公告)号:CA2329040A1

    公开(公告)日:1999-11-04

    申请号:CA2329040

    申请日:1999-04-12

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing hexanediol by hydrogenating adipic acid dialkyl esters or mixtures containing adipic acid dialkyl esters as an essential constituent and organic halogen compounds as impurities. According to said method, the adipic acid dialkyl esters or the mixtures containing adipic acid dialkyl esters are guided over copper catalysts at a temperature of 50 to 250 ~C and at a pressure of 1 to 100 bar before hydrogenation in order to remove the organic halogen compounds. Said copper catalysts contain 0.5 to 80 wt. % copper calculated as CuO and have a surface of 5 to 1500 m2/g, 0.05 to 1.5 cm3/g porosity and a copper surface of 0.1 to 20 m2/g.

    METHOD FOR PRODUCING 1,6-HEXANEDIOL

    公开(公告)号:CA2305590A1

    公开(公告)日:1999-07-08

    申请号:CA2305590

    申请日:1998-12-10

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing 1,6-hexanediol by hydrogenating adipic acid esters and/or 6-hydroxycarboxylic acid esters in the gaseous phase at an elevated temperature and pressure in the present of chromium-free catalysts. Hydrogenation is carried out a) using catalysts containing copper, manganese and aluminium as essential constituents or in the presence of Raney copper; b) at temperatures of between 150 and 230 ~C and pressures of between 10 and 70 bar; c) at a molar ratio of hyrogen to hydrogenating ester of between 150 to 1 and 300 to 1; and d) at a catalyst load of between 0.01 and 0.3 kg C3-ester per litre of catalyst and hour.

    Process for preparing polytetrahydrofuran and derivatives thereof

    公开(公告)号:AU4556497A

    公开(公告)日:1998-05-05

    申请号:AU4556497

    申请日:1997-09-23

    Applicant: BASF AG

    Abstract: PCT No. PCT/EP97/05204 Sec. 371 Date Apr. 1, 1999 Sec. 102(e) Date Apr. 1, 1999 PCT Filed Sep. 23, 1997 PCT Pub. No. WO98/15589 PCT Pub. Date Apr. 16, 1998Polytetrahydrofuran, copolymers of tetrahydrofuran and 2-butyne-1,4-diol, diesters of these polymers with C2-C20-monocarboxylic acids or monoesters of these polymers with C1-C10-monocarboxylic acids are prepared by polymerization of tetrahydrofuran in the presence of one of the telogens water, 1,4-butanediol, 2-butyne-1,4-diol, polytetrahydrofuran having a molecular weight of from 200 to 700 Dalton, a C1-C10-monocarboxylic acid or an anhydride of a C2-C20-monocarboxylic acid or a mixture of these telogens over a heterogeneous supported catalyst which comprises a catalytically active amount of an oxygen-containing molybdenum and/or tungsten compound on an oxidic support material and which has been calcined at from 5OO DEG C. to 1OOO DEG C. after application of the precursor compounds of the oxygen-containing molybdenum and/or tungsten compounds onto the support material precursor, wherein the catalyst is activated by treatment with a reducing agent before it is used as a polymerization catalyst.

    PROCESS FOR PREPARING 1,6 HEXANE DIOL WITH A LEVEL OF PURITY OVER 99 %

    公开(公告)号:CA2247991A1

    公开(公告)日:1997-09-04

    申请号:CA2247991

    申请日:1997-02-28

    Applicant: BASF AG

    Abstract: The invention relates to a process for the preparation of 1,6 hexane diol from a carboxylic acid mixture containing adipic acid, 6-hydroxy caproic acid and, in small quantities, 1,4 cyclohexane diols. Said mixture is obtained as a byproduct of the oxidation of cyclohexane into cyclohexanone/ cyclohexanol by water extraction of the reaction mixture. Said process involves esterification of the acids and hydrogenation. According to this process (a) the monocarboxylic acids and the dicarboxylic acids contained in the aqueous dicarboxylic acid mixture are reacted with a low-molecular alcohol to form the corresponding carboxylic acid esters; (b) the excess alcohol and low-boiling agents of the resultant esterification mixture are released in a first distillation stage; (c) separating into an ester fraction substantially free of 1,4 cyclohexane diols and a fraction containing at least the greater part of the 1,4 cyclohexane diols is carried out from the bottom product in a second distillation stage; (d) the ester fraction substantially free of 1,4 cyclohexane diols is catalytically hydrogenated; and (e) in a pure distillation stage 1,6 hexane diol is extracted from the hydrogenated discharge in a known manner.

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