ISOTHERMAL PROCESS FOR THE DEHYDROGENATION OF ALKANES

    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

    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

    PREPARATION OF BUTADIENE FROM N-BUTANE

    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

    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.

    PREPARATION OF BUTADIENE
    5.
    发明专利

    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

    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.

    METHOD FOR THE PRODUCTION OF PROPENE FROM PROPANE

    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

    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.

    PROCESS FOR THE PREPARATION OF ALKYLARYL COMPOUNDS AND SULFONATES THEREOF

    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

    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.

    METHOD FOR THE PRODUCTION OF BUTADIENE FROM N-BUTANE

    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

    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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