PREPARATION OF PROPENE FROM PROPANE

    公开(公告)号:MY140670A

    公开(公告)日:2010-01-15

    申请号:MYPI20060028

    申请日:2006-01-04

    Applicant: BASF AG

    Abstract: 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, IF APPROPRIATE STEAM AND, IF APPROPRIATE, AN OXYGENOUS GAS STREAM ARE FED INTO A DEHYDROGENATION ZONE AND PROPANE IS SUBJECTED TO A DEHYDROGENATION TO PROPENE TO OBTAIN A PRODUCT GAS STREAM B COMPRISING PROPANE, PROPENE, METHANE, ETHANE, ETHENE, CARBON MONOXIDE, CARBON DIOXIDE, STEAM, IF APPROPRIATE HYDROGEN AND, IF APPROPRIATE, OXYGEN; C) PRODUCT GAS STREAM B IS COOLED, IF APPROPRIATE CONDENSED AND STEAM IS REMOVED BY CONDENSATION TO OBTAIN A STEAM-DEPLETED PRODUCT GAS STREAM C; D) PRODUCT GAS STREAM C IS CONTACTED IN A FIRST ABSORPTION ZONE WITH A SELECTIVE, INERT ABSORBENT WHICH SELECTIVELY ABSORBS PROPENE TO OBTAIN AN ABSORBENT STREAM D1 LADEN SUBSTANTIALLY WITH PROPENE AND A GAS STREAM D2 COMPRISING PROPANE, METHANE, ETHANE, ETHENE, CARBON MONOXIDE, CARBON DIOXIDE AND HYDROGEN; E) IF APPROPRIATE, THE ABSORBENT STREAM D1 IS DECOMPRESSED TO A LOWER PRESSURE IN A FIRST DESORPTION ZONE TO OBTAIN AN ABSORBENT STREAM EL LADEN SUBSTANTIALLY WITH PROPENE AND A GAS STREAM E2 COMPRISING PROPENE, AND GAS STREAM E2 IS RECYCLED INTO THE FIRST ABSORPTION ZONE, F) FROM THE ABSORBENT STREAM DL OR EL LADEN SUBSTANTIALLY WITH PROPENE, IN AT LEAST ONE SECOND DESORPTION ZONE, BY DECOMPRESSION, HEATING AND/OR STRIPPING THE ABSORBENT STREAM DL OR EL, A GAS STREAM FL COMPRISING PROPENE IS RELEASED AND THE SELECTIVE ABSORBENT IS RECOVERED.

    PREPARATION OF MALEIC ANHYDRIDE
    13.
    发明专利

    公开(公告)号:MY136413A

    公开(公告)日:2008-09-30

    申请号:MYPI20042577

    申请日:2004-06-29

    Applicant: BASF AG

    Abstract: A PROCESS FOR PREPARING MALEIC ANHYDRIDE BY OXIDIZING n-BUTANE IN THE GAS PHASE UNDER HETEROGENEOUS CATALYSIS WITH OXYGEN-CONTAINING GASES OVER A VANADIUM-, PHOSPHORUS-AND OXYGEN-CONTAINING CATALYST IN A REACTOR UNIT AT A TEMPERATURE IN THE RANGE FROM 350 TO 500°C, REMOVING THE MALEIC ANHYDRIDE FORMED TO FORM A GAS STREAM WHICH COMPRISES UNCONVERTED n-BUTANE AND WATER AND RECYCLING AT LEAST A PORTION OF THE UNCONVERTED n-BUTANE TO THE REACTOR UNIT, BY FEEDING TO THE REACTOR UNIT AN INLET STREAM HAVING AN n-BUTANE CONCENTRATION OF FROM 0.5 TO 1.5BY VOLUME AND AN OXYGEN CONCENTRATION OF FROM 5 TO 21BY VOLUME, ESTABLISHING A PRESSURE AT THE INLET TO THE REACTOR UNIT OF FORM 0.4 TO 2 MPa ABS, AND CONVERTING FORM 40 TO 100OF THE n-BUTANE FROM THE INLET STREAM PER REACTOR PASS.

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