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公开(公告)号:JP2002326975A
公开(公告)日:2002-11-15
申请号:JP2002086904
申请日:2002-03-26
Applicant: BASF AG
Inventor: RHEUDE UDO , VICARI MAXIMILIAN , AQUILA WERNER , WEGNER GUENTER , NIEKERKEN JOERG
IPC: C07C67/04 , C07B61/00 , C07C67/29 , C07C67/297 , C07C69/145
Abstract: PROBLEM TO BE SOLVED: To improve a space time yield in a hydroformylation reaction of 3,4-diacetoxy-1-butene (3,4-DABE) for obtaining a C5 acetate for synthesizing vitamin A and to enhance the economic efficiency thereof. SOLUTION: This method is for producing the C5 acetate for synthesizing vitamin A by the hydroformylation of 3,4-DABE and characterized by using a 3,4-DABE-containing flow obtained by carrying out acetoxylation of 1,3-butadiene with acetic acid and air in the presence of a catalyst and extracting the 3, 4-DABE generated as a byproduct in the case by distillation.
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公开(公告)号:DE19860598A1
公开(公告)日:2000-07-06
申请号:DE19860598
申请日:1998-12-29
Applicant: BASF AG
Inventor: ADRIAN TILL , BESLING BERND , HALLMANN HEIKO , NIEKERKEN JOERG , SPINDLER VOLKER , OHLIGSCHLAEGER ANDRE , RIMPF MATTHIAS
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公开(公告)号:DE59908875D1
公开(公告)日:2004-04-22
申请号:DE59908875
申请日:1999-12-28
Applicant: BASF AG
Inventor: ADRIAN DR , BESSLING DR , HALLMANN HEIKO , NIEKERKEN JOERG , SPINDLER VOLKER , OHLIGSCHLAEGER ANDRE , RIMPF MATTHIAS
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公开(公告)号:AT261750T
公开(公告)日:2004-04-15
申请号:AT99125973
申请日:1999-12-28
Applicant: BASF AG
Inventor: ADRIAN TILL DR , BESSLING BERND DR , HALLMANN HEIKO , NIEKERKEN JOERG , SPINDLER VOLKER , OHLIGSCHLAEGER ANDRE , RIMPF MATTHIAS
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公开(公告)号:DE10033958A1
公开(公告)日:2002-01-24
申请号:DE10033958
申请日:2000-07-13
Applicant: BASF AG
Inventor: HILL THOMAS , KAIBEL GERD , MEYER GERALD , NIEKERKEN JOERG , SCHOENMAKERS HARTMUT
Abstract: Distillation apparatus, consisting of a partitioned column or a system of thermally coupled distillation columns, includes inlet lines for a hydrocarbon mixture, hydrogen and alcohol, outlet lines for low, medium and high boilers and heterogeneous hydrogenation and etherification catalysts, all located in specific segments of the apparatus. In operation hydrogen is obtained as low boiler and ether as high boiler. Distillation apparatus consists of a partitioned column or a system of thermally coupled distillation columns, including the following segments: (a) highest region of the overall arrangement; (b) concentration region of the feed unit; (c) distillation region of the feed unit; (d) upper region of the withdrawal unit; (e) lower region of the withdrawal unit; and (f) lowest region of the overall arrangement. Also provided are: a hydrocarbon mixture inlet point between segments (b) and (c); a medium boilers outlet point between (d) and (e); a low boilers outlet point in (a); a low boilers outlet point in (f); at least one hydrogen inlet point below (a); at least one alcohol inlet point in (a), (b) and/or (c); inserts containing a heterogeneous hydrogenation catalyst in (a), (d), (e) and/or (f); and inserts containing a heterogeneous etherification catalyst in (a), (b), (c) and/or (f). In operation hydrogen is obtained as low boiler and ether as high boiler. An Independent claim is included for a process for reactive distillation of hydrocarbon mixtures using the apparatus.
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公开(公告)号:MY122403A
公开(公告)日:2006-04-29
申请号:MYPI9905285
申请日:1999-12-06
Applicant: BASF AG
Inventor: ADRIAN TILL DR , BESSLING BERND DR , HALLMANN HEIKO , NIEKERKEN JOERG , SPINDLER VOLKER , GER ANDRE OHLIGSCHL XC , RIMPF MATTHIAS
Abstract: AN APPARATUS FOR CARRYING OUT DISTILLATIONS AND HETEROGENEOUSLY CATALYST REACTIONS, CONTAINING AT LEAST ONE SEGMENT WHICH HAS ALTERNATING DISTILLATION TRAYS AND REACTION TRAYS (2) ARRANGED ONE ABOVE THE OTHER, A) ONE OR MORE REACTION TRAYS (2) HAVING A REACTION ZONE WHICH CONTAINS HETEROGENEOUS CATALYST (9) AND LIQUID AND IS ARRANGED SO THAT LIQUID FLOWS THROUGH THE REACTION ZONE FROM BOTTOM TO TOP DURING THE DISTILLATION, B) THE REACTION TRAYS STATED IN A) BEING EQUIPPED WITH A FILLING AND EMPTYING MEANS FOR HETEROGENEOUS CATALYST AND C) IN EACH CASE AT LEAST ONE OUTFLOW FOR CONVEYING LIQUID BEING ARRANGED BETWEEN THE REACTION TRAYS (2) STATED IN A) AND THE RESPECTIVE NEXT LOWER DISTILLATION TRAYS, IS PREFERABLY USED FOR REACTIVE DISTILLATION.
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公开(公告)号:DE10117065A1
公开(公告)日:2002-10-10
申请号:DE10117065
申请日:2001-04-05
Applicant: BASF AG
Inventor: RHEUDE UDO , VICARI MAXIMILIAN , AQUILA WERNER , WEGNER GUENTER , NIEKERKEN JOERG
IPC: C07C67/04 , C07B61/00 , C07C67/29 , C07C67/297 , C07C69/145 , C07C67/05 , C07C67/54
Abstract: Production of C5 acetate for vitamin A synthesis is by hydroformylation of 3,4-diacetoxybutene-1 (3,4-DABE) obtained in a stream resulting from a process in which butadiene has been catalytically acetoxylated with acetic acid and air and then distilled to separate off the 3,4-DABE-containing by-product.
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