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公开(公告)号:MY136625A
公开(公告)日:2008-10-31
申请号:MYPI20045400
申请日:2004-12-29
Applicant: BASF AG
Inventor: JOHANN THORSTEN DR , SCHINDLER GOETZ-PETER DR , BRODHAGEN ANDREAS DR , CRONE SVEN DR , BENFER REGINA DR , SIGL MARCUS DR , DUDA MARK DR
IPC: C07C5/333 , C07C5/48 , C07C11/167
Abstract: The disclosure involves a process for the preparation of butadiene and 1-butene. The process includes at least a first catalytic dehydrogenation of n-butane to obtain a gas stream which is followed by at least a second oxidative dehydrogenation to form a second gas stream. The second gas stream is then subjected to distillation and isomeration steps to obtain butadiene and 1-butene.
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公开(公告)号:MY141278A
公开(公告)日:2010-04-16
申请号:MYPI20031407
申请日:2003-04-15
Applicant: BASF AG
Inventor: HOFSTADT OTTO , HESSE MICHAEL DR , SCHINDLER GOETZ-PETER DR , HARTH KLAUS DR , SIMON FALK DR
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06
Abstract: THE INVENTION RELATES TO A METHOD FOR THE PRODUCTION OF A CATALYST CARRIER, WHEREIN ZIRCONIUM DIOXIDE POWDER IS MIXED WITH A BINDING AGENT, OPTIONALLY A PORE FORMING AGENT, OPTIONALLY AN ACID, WATER AND OPTIONALLY OTHER ADDITIVES TO FORM A KNEADABLE MASS, SAID MASS IS HOMOGENIZED IN ORDER TO FORM SHAPED BODIES, DRIED AND CALCINATED. THE BINDING AGENT IS A MONOMER, OLIGOMER OR POLYMER ORGANOSILICON COMPOUND. SUITABLE BINDING AGENTS ARE MONOMER, OLIGOMER OR POLYMER SILANES, ALKOXYSILANES, ARYLOXYSILANES, ACRYLOXYSILANES, OXIMINOSILANES, HALOGENSILANES, AMINOXYSILANES, AMINOSILANES, AMIDOSILANES, SILAZANES OR SILICONES. THE INVENTION ALSO RELATES TO A CATALYST CARRIER THUS PRODUCED, A CATALYST CONTAINING SAID CARRIER AND THE USE THEREOF AS A DEHYDROGENATION CATALYST.
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公开(公告)号:MY140150A
公开(公告)日:2009-11-30
申请号:MYPI20032873
申请日:2003-07-30
Applicant: BASF AG
Inventor: SCHINDLER GOETZ-PETER DR , HARTH KLAUS DR
Abstract: ISOTHERMAL PROCESS FOR THE DEHYDROGENATION OF ALKANES Abstract Isothermal process for the dehydrogenation of alkanes to the corresponding alkenes over a catalyst bed comprising a dehydrogenation-active catalyst, wherein the catalyst bed comprises a catalytically inactive, inert diluent material. The catalytically inactive, inert diluent material is preferably selected from the group consisting of the oxides of the elements of main groups II, ill and IV, transition groups ill and IV and V, mixtures thereof and nitrides and carbides of elements of main groups ill and IV and preferably has a BET surface area of
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公开(公告)号:MY141055A
公开(公告)日:2010-02-25
申请号:MYPI20056031
申请日:2005-12-20
Applicant: BASF AG
Inventor: CRONE SVEN DR , KLANNER CATHARINA DR , SCHINDLER GOETZ-PETER DR , DUDA MARK DR , BORGMEIER FRIEDER DR
Abstract: A PROCESS FOR PREPARING BUTADIENE FROM N-BUTANE, COMPRISING THE STEPS OF A) PROVIDING A FEED GAS STREAM A COMPRISING N-BUTANE; B) FEEDING THE FEED GAS STREAM A COMPRISING N-BUTANE INTO AT LEAST ONE FIRST DEHYDROGENATION ZONE AND NONOXIDATIVELY, CATALYTICALLY DEHYDROGENATING N-BUTANE TO OBTAIN A GAS STREAM B COMPRISING N-BUTANE, 1-BUTENE, 2-BUTENE, BUTADIENE AND HYDROGEN, WITH OR WITHOUT STEAM, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES; C) FEEDING THE GAS STREAM B AND AN OXYGENOUS GAS INTO AT LEAST ONE SECOND DEHYDROGENATION ZONE AND OXIDATIVELY DEHYDROGENATING 1-BUTENE AND 2-BUTENE TO OBTAIN A GAS STREAM C COMPRISING N-BUTANE, BUTADIENE, HYDROGEN, STEAM, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES; D) COMPRESSING IN AT LEAST ONE FIRST COMPRESSION STAGE AND COOLING THE GAS STREAM C TO OBTAIN AT LEAST ONE CONDENSATE STREAM D1 COMPRISING WATER AND A GAS STREAM D2 COMPRISING N-BUTANE, BUTADIENE, HYDROGEN AND STEAM, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES; E) SEPARATING THE GAS STREAM D2 BY EXTRACTIVE DISTILLATION INTO A PRODUCT STREAM E1 CONSISTING SUBSTANTIALLY OF BUTADIENE AND A STREAM E2 COMPRISING N-BUTANE, HYDROGEN AND STEAM, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES; F) IF APPROPRIATE COMPRESSING IN ONE OR MORE FURTHER COMPRESSION STAGES AND COOLING THE GAS STREAM E2 TO OBTAIN AT LEAST ONE CONDENSATE STREAM F1 COMPRISING N-BUTANE AND WATER, AND A GAS STREAM F2 COMPRISING N-BUTANE AND HYDROGEN, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES, AND IF APPROPRIATE RECYCLING THE CONDENSATE STREAM F1 INTO THE FIRST DEHYDROGENATION ZONE; G) SEPARATING THE GAS STREAM 12 INTO A RECYCLE STREAM G1 COMPRISING N-BUTANE AND AN 011GAS STREAM G2 COMPRISING HYDROGEN, WITH OR WITHOUT CARBON OXIDES AND WITH OR WITHOUT INERT GASES, BY CONTACTING THE GAS STREAM 12 WITH A HIGH-BOILING ABSORBENT AND SUBSEQUENTLY DESORBING THE GAS CONSTITUENTS DISSOLVED IN THE ABSORBENT.
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公开(公告)号:MY140092A
公开(公告)日:2009-11-30
申请号:MYPI20045270
申请日:2004-12-21
Applicant: BASF AG
Inventor: JOHANN THORSTEN DR , SCHINDLER GOETZ-PETER DR , BRODHAGEN ANDREAS DR , CRONE SVEN DR , BENFER REGINA DR , HILL THOMAS DR , DUDA MARK DR
IPC: C07C5/327 , C07C5/333 , C07C5/48 , C07C11/167
Abstract: The disclosure relates to a process for preparing butadiene. The process involves nonoxidatively catalytically dehydrogenating butane to obtain a product gas stream containing butane, 1-butene, 2-butene, butadiene, hydrogen and secondary constituents. The 1-butene and 2-butene of the product gas stream is then oxidatively dehydrogenated to give a second gas stream containing butane,2-butene, butadiene, hydrogen, steam and secondary constituents. Next, the butane,2-butene and butadiene are separated from the second gas stream and the butane and 2-butene are then separated from the butadiene product. The butane and 2-butene are then recycled into the nonoxidative catalytic dehydrogenating zone.
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公开(公告)号:CZ20024057A3
公开(公告)日:2003-05-14
申请号:CZ20024057
申请日:2001-06-08
Applicant: BASF AG
Inventor: MACHHAMMER OTTO DR , SCHINDLER GOETZ-PETER DR , TENTEN ANDREAS DR , HARTH KLAUS DR , ZEHNER PETER DR , MULLER-ENGEL KLAUS JOACHIM DR , ROSOWSKI FRANK DR , BORGMEIER FRIEDER DR
IPC: C07C27/14 , C07B61/00 , C07C5/333 , C07C11/06 , C07C45/33 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/04 , C07C57/05 , C07C57/07
Abstract: In a process for the preparation of acrolein or acrylic acid or a mixture thereof from propane, the propane is subjected, in a first reaction stage, to a partial dehydrogenation under heterogeneous catalysis to give propene, of the components contained in the product gas mixture formed in the first reaction stage other than propene and propane at least a portion of the molecular hydrogen present is then separated off from said mixture and the product gas mixture is then used for the preparation of acrolein and/or acrylic acid by gas-phase catalytic propylene oxidation, molecular nitrogen being present for diluting the reaction gas mixture during the propylene oxidation.
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公开(公告)号:MY147177A
公开(公告)日:2012-11-14
申请号:MYPI20056086
申请日:2005-12-21
Applicant: BASF AG
Inventor: CRONE SVEN DR , MACHHAMMER OTTO DR , SCHINDLER GOETZ-PETER DR
IPC: C07C5/333
Abstract: THE INVENTION RELATES TO A PROCESS FOR PREPARING PROPENE FROM PROPANE, COMPRISING THE STEPS: A) A FEED GAS STREAM A COMPRISING PROPANE IS PROVIDED; B) THE FEED GAS STREAM A COMPRISING PROPANE AND AN OXYGENOUS GAS STREAM ARE FED INTO A DEHYDROGENATION ZONE AND PROPANE IS SUBJECTED TO A NONOXIDATIVE CATALYTIC, AUTOTHERMAL DEHYDROGENATION TO PROPENE TO OBTAIN A PRODUCT GAS STREAM B COMPRISING PROPANE, PROPENE, METHANE, ETHANE, ETHENE, NITROGEN, CARBON MONOXIDE, CARBON DIOXIDE, STEAM AND HYDROGEN; C) PRODUCT GAS STREAM B IS COOLED AND STEAM IS REMOVED BY CONDENSATION TO OBTAIN A STEAM-DEPLETED PRODUCT GAS STREAM C; D) UNCONDENSABLE OR LOW-BOILING GAS CONSTITUENTS ARE REMOVED BY CONTACTING PRODUCT GAS STREAM C WITH AN INERT ABSORBENT AND SUBSEQUENTLY DESORBING THE GASES DISSOLVED IN THE INERT ABSORBENT TO OBTAIN A C3 HYDROCARBON STREAM D1 AND AN OFFGAS STREAM D2 COMPRISING METHANE, ETHANE, ETHENE, NITROGEN, CARBON MONOXIDE, CARBON DIOXIDE AND HYDROGEN; E) THE C3 HYDROCARBON STREAM D1 IS COOLED AND COMPRESSED TO OBTAIN A LIQUID C3 HYDROCARBON STREAM E1; F) THE LIQUID C3- HYDROCARBON STREAM E1 IS FED INTO A FIRST DISTILLATION ZONE AND SEPARATED DISTILLATIVELY INTO A STREAM F1 COMPOSED OF PROPANE AND PROPENE AND A STREAM F2 COMPRISING ETHANE AND ETHENE; G) STREAM F1 IS FED INTO A (SECOND) DISTILLATION ZONE AND SEPARATED DISTILLATIVELY INTO A PRODUCT STREAM G1 COMPOSED OF PROPENE AND A STREAM G2 COMPOSED OF PROPANE, AND STREAM G2 IS RECYCLED AT LEAST PARTLY INTO THE DEHYDROGENATION ZONE.
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公开(公告)号:MY139380A
公开(公告)日:2009-09-30
申请号:MYPI20023670
申请日:2002-10-01
Applicant: BASF AG
Inventor: STEINBRENNER ULRICH DR , HEIDEMANN THOMAS DR , SCHINDLER GOETZ-PETER DR , STEPHAN JUERGEN DR , MAAS HEIKO DR
IPC: C07C15/00 , C07C309/31 , C11D1/22
Abstract: THE PREPARATION OF ALKYLARYL COMPOUNDS TAKES PLACE, INTER ALIA, BYA1) PREPARATION OF C4-OLEFIN MIXTURE FROM LPG, LNG OR MTO STREAMS,@B1) REACTION OF THE C4-OLEFIN MIXTURE OBTAINED IN THIS WAY OVER A METATHESIS CATALYST FOR THE PREPARATION OF AN OLEFIN MIXTURE COMPRISING 2-PENTENE AND/ OR 3-HEXENE AND OPTIONAL REMOVAL OF 2-PENTENE AND/ OR 3-HEXENE,CI) DIMERIZATION OF THE 2-PENTENE AND/OR 3-HEXENE OBTAINED IN STAGE B1) OVER A DIMERIZATION CATALYST TO GIVE A MIXTURE COMPRISNG C10-12 OLEFINS,D1) REACTION OF THE C10-12 OLEFIN MIXTURE OBTAINED IN STAGE B1) WITH AN AROMATIC HYDROCARBON IN THE PRESENCE OF AN ALKYLATION CATALYST TO FORM ALKYLAROMATIC COMPOUNDS, IT BEING POSSIBLE TO ADD ADDITIONAL LINEAR OLEFINS PRIOR TO THE REACTION.
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公开(公告)号:MY139227A
公开(公告)日:2009-08-28
申请号:MYPI20030701
申请日:2003-02-27
Applicant: BASF AG
Inventor: MACHHAMMER OTTO DR , SCHINDLER GOETZ-PETER DR , HARTH KLAUS DR , ZEHNER PETER DR
IPC: B01J23/62 , C07C5/327 , B01J8/02 , B01J19/26 , B01J27/199 , C07B61/00 , C07C5/333 , C07C11/06 , C07C11/08 , C07C11/09 , C07C45/33 , C07C45/35
Abstract: A PROCESS FOR THE CONTINUOUS HETEROGENEOUSLY CATALYZED PARTIAL DEHYDROGENATION OF A HYDROCARBON IN THE GAS PHASE AND IN THE PRESENCE OF MOLECULAR OXYGEN, IN WHICH PART OF THE PRODUCT GAS (5) IS RECIRCULATED TO THE REACTION ZONE, AND A REACTOR FOR CARRYING OUT SUCH A PROCESS. (FIGURE 2)
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公开(公告)号:MY135793A
公开(公告)日:2008-06-30
申请号:MYPI20032539
申请日:2003-07-07
Applicant: BASF AG
Inventor: SCHINDLER GOETZ-PETER DR , WALSDORFF CHRISTIAN DR , HARTH KLAUS DR , HIBST HARTMUT PROF DR
IPC: B01J23/62 , C07C5/333 , C07B61/00 , C07C11/167
Abstract: THE INVENTION RELATES TO A PROCESS FOR PREPARING BUTADIENE FROM N-BUTANE COMPRISING THE STEPS (A) PROVIDING AN N-BUTANE-CONTAININGFEED GAS STREAM,(B) FEEDING THE N-BUTANE-CONTAINING FEED GAS STREAM INTO A FIRST DEHYDROGENATION ZONE AND NONOXIDATIVELY CATALYTICALLY DEHYDROGENATING N-BUTANE TO 1-BUTENE, 2-BUTENE AND OPTIONALLY BUTADIENE TO OBTAIN A FIRST PRODUCT GAS STREAM COMPRISING N-BUTANE,1-BUTENE AND 2-BUTENE, WITH OR WITHOUT BUTADIENE AND SECONDARY COMPONENTS, (C) FEEDING THE FIRST PRODUCT GAS STREAM COMPRISING N-BUTANE, 1-BUTENE AND 2-BUTENE,WITH OR WITHOUT BUTADIENE AND SECONDARY COMPONENTS, INTO A SECOND DEHYDROGENATION ZONE AND OXIDATIVELY DEHYDROGENATING 1-BUTENE AND 2-BUTENE TO BUTADIENE TO GIVE A SECOND PRODUCT GAS STREAM COMPRISING BUTADIENE, N-BUTANE AND STEAM, WITH OR WITHOUT SECONDARY COMPONENTS, (D) RECOVERING BUTADIENE FROM THE SECOND PRODUCT GAS STREAM.
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