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公开(公告)号:CA2180982A1
公开(公告)日:1995-07-20
申请号:CA2180982
申请日:1995-01-12
Applicant: BASF AG
Inventor: KANAND JUERGEN , ROEPER MICHAEL , PINKOS ROLF , PACIELLO ROCCO , 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: In a process for producing n-butyraldehyde and/or n-butanol, (a) 1,3-butadiene is reacted with an alcohol having the formula ROH, in which the residue R stands for a non-substituted C2-C20-alkyl or alkenyl group that may also be substituted by 1 or 2 C1-C10-alkoxy or hydroxy groups, a C6-C10-aryl or C7-C11-aralkyl group or the methyl group, at a higher temperature and pressure in the presence of a Brönsted acid or in the presence of a compound of an element from groups IB, VIIb or VIIIb of the periodic table of elements with phosphoric or nitrogenated ligands, so as to produce a mixture of addition compounds having the formulas (II) and (III); (b) the addition compound III is isomerised into the addition compound II; (c) the addition compound II is isomerised in the presence of a homogeneous or heterogeneous transition metal element catalyst in liquid phase or in the presence of a heterogeneous transition metal element-containing catalyst in gaseous phase, so as to produce an enol ether having the formula (IV); and (d) n-butyraldehyde and/or n-butanol are generated by reacting said enol ether IV with hydrogen and water or with water in the presence of a homogeneous or heterogeneous transition metal element catalyst in the liquid phase or in the presence of a heterogeneous transition metal element-containing catalyst in the gaseous phase. The alcohol ROH released is recycled into the partial reaction (a).
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公开(公告)号:CA2168458A1
公开(公告)日:1995-02-09
申请号:CA2168458
申请日:1994-07-07
Applicant: BASF AG
Inventor: PINKOS ROLF , FISCHER ROLF HARTHMUTH , BREITSHCEIDEL BORIS , POLANEK PETER
IPC: B01J23/36 , B01J23/46 , B01J23/72 , B01J23/889 , B01J31/22 , C07B61/00 , C07C29/00 , C07C29/10 , C07C29/132 , C07C29/17 , C07C31/20 , C07D307/20 , C07D307/28
Abstract: In the proposed process for producing 1,4 butane diol, 2,5 dihydrofurane is reacted in a single step in the presence of water and hydrogen at a temperature of 20 to 300 .degree.C and a pressure of 1 to 300 bar with the aid of a hydrogenating catalyst.
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公开(公告)号:AU2006263876B2
公开(公告)日:2010-11-04
申请号:AU2006263876
申请日:2006-06-26
Applicant: BASF AG
Inventor: PINKOS ROLF , KARL JORN , SCHELLING HEINER , EIERMANN MATTHIAS , STROFER ECKHARD , TEBBEN GERD-DIETER , HAUNERT ANDREA
Abstract: A biodiesel fuel mixture having a cetane number of >40, comprising a) from 1 to 100% by weight of biodiesel, b) from 0 to 98.9% by weight of diesel oil of fossil origin, c) from 0.1 to 20% by weight of polyoxyalkylene dialkyl ether of the formula RO(CH 2 O) n R in which R is an alkyl group having from 1 to 10 carbon atoms and n=from 2 to 10, and d) from 0 to 5% by weight of further additives.
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公开(公告)号:PT1646604E
公开(公告)日:2008-02-11
申请号:PT04740321
申请日:2004-06-25
Applicant: BASF AG
Inventor: PINKOS ROLF , STROEFER ECKHARD , DEBERDT FILIP , STEINBRENNER ULRICH , SOHN MARTIN , QUASCHNING VERONIKA , MOEHWALD HELMUT , THIELE KAI , JACOBS JAN D
IPC: C07C209/78 , C07C209/86 , C07C211/50
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公开(公告)号:DE102006024903A1
公开(公告)日:2007-11-29
申请号:DE102006024903
申请日:2006-05-24
Applicant: BASF AG
Inventor: PINKOS ROLF , KAIBEL GERD , DAHLHOFF ELLEN , WINDECKER GUNTHER , HEIMANN JENS
IPC: C07D307/60 , C07C55/10
Abstract: The present invention provides a process for preventing fumaric acid deposits in the preparation of maleic anhydride, comprising the following steps: a) absorption of a C4-dicarboxylic acid or of a derivative from a crude product mixture into an organic solvent or water as an absorbent, b) removal of the C4-dicarboxylic acid or of a derivative from the absorbent, the absorbent thus recovered being catalytically hydrogenated fully or partly and recycled fully or partly into the absorption stage (a).
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66.
公开(公告)号:MY133071A
公开(公告)日:2007-10-31
申请号:MYPI9805291
申请日:1998-11-20
Applicant: BASF AG
Inventor: PAUL AXEL , STEIN FRANK , FISCHER ROLF HARTMUTH , PINKOS ROLF , KRUG THOMAS
Abstract: A PROCESS FOR THE CATALYTIC HYDROGENATION OF CARBOXYLIC ACIDS OF ANHYDRIDES OR ESTERS THEREOF TO ALCOHOLS OVER HETEROGENEOUS CATALYSTS WHICH COMPRISE OR CONSIST OF HYDROGENARATING ELEMENTS FROM GROUPS 6, 7, 8, 9, 10 AND 11 AND, WHERE APPROPRIATE, FROM GROUPS 2, 14 AND 15 OF THE PERIODIC TABLE OF THE ELEMENTS IN LIQUID PHASE AT FROM 100 TO 300°C AND FROM 10 TO 300 BAR WHICH COMPRISES ADDING FROM 1 TO 3000 PPM, BASED ON THE LIQUID HYDROGENATION FEED, OF A BASIC ALKALI METAL COMPOUND OR ALKALINE EARTH METAL COMPOUND SELECTED FROM THE GROUP CONSISTING OF HYROXIDES, CARBONATES, CARBOXYLATES AND ALKOXIDES TO THE HYDROGENATION REACTION MIXTURE.
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公开(公告)号:CA2297724C
公开(公告)日:2007-10-09
申请号:CA2297724
申请日:1998-10-16
Applicant: BASF AG
Inventor: STEIN FRANK , PINKOS ROLF , FISCHER ROLF HARTMUTH
IPC: C07C29/149 , C07B61/00 , C07C29/80 , C07C31/20 , C07C51/367 , C07C62/02 , C07C67/31 , C07C69/675
Abstract: The invention relates to a method for producing 1,6-hexanediol and 6- hydroxycaproic acid or their esters by the catalytic hydrogenation of adipic acid, adipic acid monoesters or adipic acid diesters or educt flow s containing adipic acid or its esters as essential constituents. The bottom product obtained when the hydrogenation discharge is distilled after the hexanediol and the hydroxycaproic acid or its esters have been separated off is reintroduced into the hydrogenation process, said bottom product essentially containing oligomeric esters of the 6-hydroxycaproic acid. The resulting mixture of the educt and the return flo w is reacted at temperatures of 100 to 300 .degree.C and at pressures of 10 to 300 bar in the liquid phase and with a molar ratio of carboxyl grou ps to be hydrogenated to hydrogen in the reactor of 1:5 to 1:100, on hydrogenating catalysts.
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公开(公告)号:DE102006009150A1
公开(公告)日:2007-09-06
申请号:DE102006009150
申请日:2006-02-24
Applicant: BASF AG
Inventor: PINKOS ROLF , KAESHAMMER STEFAN , GRAF HERMANN , RODEWALD DIETER , WABNITZ TOBIAS , HATSCHER STEPHAN
Abstract: A linear aliphatic ether is present at 0.001-5 wt.% in the reaction mixture when polytetrahydrofuran or a tetrahydrofuran (THF) copolymer is produced by polymerization of THF with an acid catalyst in presence of a telogen and/or a comonomer.
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公开(公告)号:AU2006263876A1
公开(公告)日:2007-01-04
申请号:AU2006263876
申请日:2006-06-26
Applicant: BASF AG
Inventor: PINKOS ROLF , KARL JORN , SCHELLING HEINER , EIERMANN MATTHIAS , STROFER ECKHARD , TEBBEN GERD-DIETER , HAUNERT ANDREA
Abstract: A biodiesel fuel mixture having a cetane number of >40, comprising a) from 1 to 100% by weight of biodiesel, b) from 0 to 98.9% by weight of diesel oil of fossil origin, c) from 0.1 to 20% by weight of polyoxyalkylene dialkyl ether of the formula RO(CH 2 O) n R in which R is an alkyl group having from 1 to 10 carbon atoms and n=from 2 to 10, and d) from 0 to 5% by weight of further additives.
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公开(公告)号:CA2247991C
公开(公告)日:2006-06-27
申请号:CA2247991
申请日:1997-02-28
Applicant: BASF AG
Inventor: BREITSCHEIDEL BORIS , FISCHER ROLF , PINKOS ROLF , RUST HARALD , STEIN FRANK , BAUR KARL GERHARD
IPC: C07C31/20 , C07C29/149
Abstract: The invention relates to a process for the preparation of 1,6 hexane diol fr om 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 by-product 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 an d 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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