PREPARATION OF PROPENE FROM PROPANE

    公开(公告)号:MY144056A

    公开(公告)日:2011-08-15

    申请号:MYPI20055753

    申请日:2005-12-08

    Applicant: BASF AG

    Abstract: - 23 - PREPARATION OF PROPME FROM.-PROPANE ABSTIACT THE INVENTION RELATES TO A PROCESS FOR PIEPARIN,O PIOPENE FROM PROPANE, COMPRISING THE 5 STEPS: A) A FEED GAS SIREARN A COMPSING PROPANE IS PROVIDED; B) THE FEED PAS STREAM A COMPRISING PROPANE AND AN OXYGENOUS -AS STREARN ARE FED 10 INTO A DEHYDRO.-ENATION ZONE AND PROPANE IS SUBJECTED TO A NONOXIDATIVE CAIALYLIC, AUTOTHEIRRIAL DCHYDROGENATION TO PROPENE TO OBTAIN A PI ODUCI GAS STREAM B CORNPRIS- ING PROPANE, PIOPENE, METHANE. ETHANE. ETHENE, C4' HYDROCWBOJIS, CARBON NIONOX- IDE, CAIBON DIOXIDE, STEAM AND LWDRO2CN, 15 Q THE PRODUCT OAS STREAM B IS COOLED AND SICAM IS IERNOVED BY CONDENS3TION LO OB- IAIN A SICARRI-DEPLETED PRODUCT GAS STICARN C, D) CARBON DIOXIDE IS IENIOVED BY OAS SCRUBBJN2 TO OBTAIN A CARBON DIOXIDE-DEPLETED PRODUCT GAS STREAM D, 20 E) THC PRODUCT -AS STICARN D IS COOLED AND A LIQUID HYDIOCAIBON STREAM EL CORNPLISINO PROPANE, PROPENE, METHANE, ETHANE. ETHERIC AND C@' LI@,DROCARBONS IS IEMOVED BN CONDENSATION IO LEAVE A RESIDUAL GAS STREAM E2 CORNPIISIN.- METHANE, HYDJO,GEN AND CARBON MONOXIDE. 25 F) THE LIQUID HYDROCARBON STREAM EL IS FED INTO A FIRST DISTILLATION ZONE AND SEPARATED DISTILLAIIVELY INTO A STREAM 1-1 COMPIISING PROPANE. PROPENE AND THE C4' HYDIOCAR- BONS AND A STREAM 1`2 COMPRISING ETHANE AND CIHENE. 30 G) THE STICARN FJ IS FED INTO A SECOND DISIFLLANON ZONE AND SEPARATED DISTILLANVELY INTO A PIODUCT STREAM 21 CORNPIISIN2 PROPENE AND A STREAM G2 COMPIISING PROPANE AND THE C4' HYDI OCAI BONS.

    METHOD FOR THE PRODUCTION OF BUTADIENE FROM N-BUTANE

    公开(公告)号:MY140931A

    公开(公告)日:2010-02-12

    申请号:MYPI20055754

    申请日:2005-12-08

    Applicant: BASF AG

    Abstract: A PROCESS FOR PREPARING BUTADIENE, COMPRISING NONOXIDATIVELY DEHYDROGENATING N-BUTANE FROM A STREAM (4) (A) IN A FIRST DEHYDROGENATION ZONE (18) TO OBTAIN STREAM (5) (B) COMPRISING I-BUTENE AND 2-BUTENE; OXIDATIVELY DEHYDROGENATING THE I-BUTENE AND 2-BUTENE OF (B) IN THE PRESENCE OF AN OXYGENOUS GAS (6) IN A SECOND DEHYDROGENATION ZONE (19) TO OBTAIN STREAM (C) COMPRISING N-BUTANE, BUTADIENE, HYDROGEN, CARBON DIOXIDE, AND STEAM; COMPRESSING (21) AND COOLING (C) TO OBTAIN STREAM (D2) COMPRISING N-BUTANE, BUTADIENE, HYDROGEN, CARBON DIOXIDE, AND STEAM; EXTRACTIVELY DISTILLING (22) (D2) INTO STREAM (E1) COMPRISING BUTADIENE AND STREAM (E2) COMPRISING N-BUTANE, HYDROGEN, CARBON DIOXIDE, AND STEAM; COMPRESSING (23, 24) AND COOLING (E2) TO OBTAIN STREAM (FL) COMPRISING N-BUTANE AND WATER AND STREAM (F2) COMPRISING N-BUTANE, HYDROGEN, AND CARBON DIOXIDE; COOLING (F2) TO OBTAIN STREAM (G1) COMPRISING N-BUTANE AND STREAM (G2) COMPRISING CARBON DIOXIDE AND HYDROGEN; PHASE SEPARATING WATER FROM (FL) TO OBTAIN STREAM (H1) COMPRISING N-BUTANE; AND RECYCLING (HI) INTO THE FIRST DEHYDROGENATION ZONE (18).

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