-
公开(公告)号:CA2598585A1
公开(公告)日:2006-08-31
申请号:CA2598585
申请日:2006-02-24
Applicant: BASF AG
Inventor: MALTRY MICHAELA , DIEHLMANN UWE , HEIDEMANN THOMAS , STEPHAN JUERGEN , POPLOW FRANK , SCHUBERT MARKUS
Abstract: Preparation of non-aromatic carbon-carbon double/triple bond compound (A) or its mixtures from another non-aromatic carbon-carbon double/triple bond compound (B), comprises reacting pure (B) with an adsorption agent comprising an aluminum oxide (3 wt.%) and activating at 450-1000[deg]C; and contacting the pure compound (B) with a metathesis catalyst.
-
公开(公告)号:DE102004049940A1
公开(公告)日:2006-04-20
申请号:DE102004049940
申请日:2004-10-13
Applicant: BASF AG
Inventor: STEPHAN JUERGEN , BRODHAGEN ANDREAS , SCHUBERT MARKUS , POPLOW FRANK , ROEPER MICHAEL , HILL THOMAS
Abstract: A C4-olefin mixture having a 1,3-butadiene content of from 100 to 500 ppm and a content of 1,2-dienes of less than 10 ppm is described. The present invention further provides a process for preparing this C4-olefin mixture and provides for its use in a metathesis reaction for preparing 2-pentene and/or 3-hexene.
-
公开(公告)号:DE102004041850A1
公开(公告)日:2006-03-02
申请号:DE102004041850
申请日:2004-08-27
Applicant: BASF AG
Inventor: SIGL MARKUS , SCHUBERT MARKUS , STEPHAN JUERGEN , PAPP RAINER , POPLOW FRANK
Abstract: Processes for preparing a C5 aldehyde and propene are disclosed, the processes comprising: (a) providing a feedstream, the feedstream comprising butane, 1-butene, 2-butene and 1,3-butadiene, the 1,3-butadiene present in the feedstream in an amount up to 1000 ppm; (b) contacting the feedstream with hydrogen and carbon monoxide in the presence of a hydroformylation catalyst to form a 2-butene-rich butane stream and a C5 aldehyde; (c) separating the 2-butene-rich butane stream and the C5 aldehyde; and (d) contacting the 2-butene-rich butane stream with ethene in the presence of a metathesis catalyst to form a propene-containing hydrocarbon stream.
-
公开(公告)号:CA2557345A1
公开(公告)日:2005-09-09
申请号:CA2557345
申请日:2005-02-24
Applicant: BASF AG
Inventor: STEPHAN JUERGEN , BRODHAGEN ANDREAS , BOEHM VOLKER , SCHUBERT MARKUS , POPLOW FRANK
Abstract: Process for producing a supported catalyst which comprises at least 75% by weight of Al 2 O 3 , whose proportion of Al 2 O 3 in the delta or theta modification is, based on the proportion of Al 2 O 3 , at least 1% and which comprises a rhenium compound and, if appropriate, a promoter as active component (A), which comprises a) converting a customary support (S) which comprises at least 75% by weight of Al 2 O 3 and to which a promoter may, if appropriate, have been applied is converted into a modified support (S) whose proportion of Al 2 O 3 in the delta or theta modification is, based on the proportion of Al 2 O 3 , at least 1% by calcining the customary support (S) at a temperature of from 750 to 1100°C., b) producing a supported catalyst precursor from the modified support (S) by applying the active component (A) comprising the rhenium compound to the modified support (S) and c) calcining the supported catalyst precursor at a temperature of from 500 to 750° C.
-
公开(公告)号:DE59907200D1
公开(公告)日:2003-11-06
申请号:DE59907200
申请日:1999-04-12
Applicant: BASF AG
Inventor: PENZEL ULRICH , SCHARR VOLKER , STAROSTA DIETER , BOESEL HILMAR , STROEFER ECKHARD , PFEFFINGER JOACHIM , POPLOW FRANK , DOSCH JUERGEN , SCHWARZ VOLKMAR , NAEUMANN FRITZ , VAN DEN ABEEL PETER , JACOBS JAN , NEVEJANS FILIP , VAN PEE WILLY
IPC: C07C263/10 , C07C263/20 , C07C265/14
Abstract: In a process for preparing mixtures of diphenylmethane diisocyanates and polyphenylpolymethylene polyisocyanates having a reduced content of chlorinated by-products and a reduced iodine color number by two-stage reaction of the corresponding mixtures of diphenylmethanediamines and polyphenylpolymethylenepolyamines with phosgene in the presence of at least one inert organic solvent at elevated temperature, separation of the excess phosgene and solvent after the phosgenation is complete and thermal treatment of the reaction product, the mass ratios of phosgene to hydrogen chloride in the residence time apparatus of the second stage of the phosgenation are at the same time 10-30:1 in the liquid phase and 1-10:1 in the gas phase.
-
公开(公告)号:DE502005002594D1
公开(公告)日:2008-03-06
申请号:DE502005002594
申请日:2005-08-06
Applicant: BASF AG
Inventor: SIGL MARCUS , SCHUBERT MARKUS , STEPHAN JUERGEN , PAPP RAINER , POPLOW FRANK
Abstract: Processes for preparing a C5 aldehyde and propene are disclosed, the processes comprising: (a) providing a feedstream, the feedstream comprising butane, 1-butene, 2-butene and 1,3-butadiene, the 1,3-butadiene present in the feedstream in an amount up to 1000 ppm; (b) contacting the feedstream with hydrogen and carbon monoxide in the presence of a hydroformylation catalyst to form a 2-butene-rich butane stream and a C5 aldehyde; (c) separating the 2-butene-rich butane stream and the C5 aldehyde; and (d) contacting the 2-butene-rich butane stream with ethene in the presence of a metathesis catalyst to form a propene-containing hydrocarbon stream.
-
公开(公告)号:CA2598322A1
公开(公告)日:2006-08-31
申请号:CA2598322
申请日:2006-02-24
Applicant: BASF AG
Inventor: SIGL MARCUS , SCHUBERT MARKUS , STEPHAN JURGEN , POPLOW FRANK
Abstract: Preparation of an ethene stream (C 2), a propene stream (C 3), an isobutene and optionally a 4C-olefin stream (C 4), a 2-methyl-2-butene and optionally 2-butene stream (C 5), and optionally other hydrocarbons containing stream (C x), optionally several separate components containing streams, comprises contacting a C4-hydrocarbon stream with ethene in a metathesis step; and separating the streams. Preparation of an ethene stream (C 2), a propene stream (C 3), an isobutene and optionally 4C olefin stream (C 4), a 2-methyl-2-butene and optionally 2-butene stream (C 5), and optionally other hydrocarbons containing stream (C x), optionally several separate components containing streams, comprises: (A) a metathesis step, in which a C4-hydrocarbon stream, containing at least 2-butene (15 wt.%), at least isobutene (5 wt.%) and 1-butene (less than 5 wt.%) (feed stream), is contacted with ethene in the presence of usual metathesis catalysts; and (B) separation of the streams (C2, C3, C4 and optionally Cx) from the obtained hydrocarbon stream, with the stream (C5) completely or partially led back to the metathesis step. Independent claims are included for methods for preparing feed stream, comprising subjecting naphtha or other hydrocarbon compounds to steam cracking or fluid catalytic cracking (FCC)-process, or dehydrating butane containing hydrocarbon stream and followed by purifying the obtained C4-olefin-mixture containing isobutene, 2-butene, butadiene, optionally butyne and optionally 1-butene, and removing the obtained stream of C4-olefin-mixture; and removing butadiene and butyne by means of selective hydrogenation to butene or butane hydride, or butadiene and butyne by extractive distillation of the obtained C4-olefin-mixture (raffinate I), where the content of 1,3-butadiene is at a maximum of 1000 wt. ppm.
-
公开(公告)号:CA2584235A1
公开(公告)日:2006-04-20
申请号:CA2584235
申请日:2005-10-13
Applicant: BASF AG
Inventor: SCHUBERT MARKUS , HILL THOMAS , BRODHAGEN ANDREAS , STEPHAN JUERGEN , POPLOW FRANK , ROEPER MICHAEL
IPC: C07C5/05 , C07C6/04 , C07C11/08 , C07C11/10 , C07C11/107
Abstract: A C4-olefin mixture having a 1,3-butadiene content of from 100 to 500 ppm and a content of 1,2-dienes of less than 10 ppm is described. The present invention further provides a process for preparing this C4-olefin mixture and provides for its use in a metathesis reaction for preparing 2-pentene and/or 3-hexene.
-
公开(公告)号:DE10319437A1
公开(公告)日:2004-11-18
申请号:DE10319437
申请日:2003-04-30
Applicant: BASF AG
Inventor: SCHUBERT MARKUS , GERLACH TILL , HESSE MICHAEL , STEPHAN JUERGEN , BOEHM VOLKER , BRODHAGEN ANDREAS , POPLOW FRANK
Abstract: Preparation of unsaturated compounds having a non-aromatic C-C double or triple bond (compound A) from another compound or a mixture of other compounds having a non-aromatic C-C double or triple bond (compound B), includes bringing the compound (B) into contact with a heterogeneous catalyst comprising carbides or oxycarbides of a transition element at 50-500[deg]C.
-
30.
公开(公告)号:DE19817691A1
公开(公告)日:1999-10-28
申请号:DE19817691
申请日:1998-04-21
Applicant: BASF AG
Inventor: PENZEL ULRICH , SCHARR VOLKER , STAROSTA DIETER , BOESEL HILMAR , STROEFER ECKHARD , PFEFFINGER JOACHIM , ABEEL PETER VAN DEN , JACOBS JAN , NEVEJANS FILIP , POPLOW FRANK , DOSCH JUERGEN , SCHWARZ HANS VOLKMAR , NAEUMANN FRITZ , PEE WILLY VAN
IPC: C07C263/10 , C07C263/20 , C07C265/14
Abstract: Surprisingly, the drawbacks of previous processes for the preparation of mixtures containing diphenylmethanediisocyanate and polyphenylene-polymethylene-polyisocyanate, e.g. high cost, excessive HCl stripping time, can be avoided by a two-stage reaction of corresponding mixtures containing diphenylmethane-diamine and polyphenylene-polymethylene-polyamine with phosgene in the presence of inert organic solvent. Mixtures containing diphenylmethanediisocyanate and polyphenylene-polymethylene-polyisocyanate (PMDI) having a decreased content of chlorinated side product and decreased iodine colour index are obtained by two-stage reaction of corresponding mixtures containing diphenylmethanediamine and polyphenylene-polymethylene-polyamine (PMDA) with phosgene in the presence of at least one inert organic solvent. The weight ratio of phosgene to HCl in the dwell time apparatus of the second phosgenation stage is (10-30):1 in the liquid phase and (1-10):1 in the gas phase. An Independent claim is included for mixtures containing diphenylmethanediisocyanate and PMDI obtainable by the above process.
-
-
-
-
-
-
-
-
-