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公开(公告)号:MY125936A
公开(公告)日:2006-09-29
申请号:MYPI20005923
申请日:2000-12-15
Applicant: BASF AG
Inventor: BLOCK ULRICH DR , SEUBERT ROLF DR , ULRICH BERNHARD DR , WUNSCHMANN HELMUT
IPC: B01F23/10
Abstract: A PROCESS AND APPARATUS FOR PRODUCING A HOMOGENEOUS MIXTURE OF A GASEOUS AROMATIC HYDROCARBON AND AN OXYGEN-CONTAINING GAS FOR CATALYTIC GAS-PHASE REACTIONS, IN PARTICULAR A HOMOGENEOUS MIXTURE OF GASEOUS O-XYLENE AND/OR NAPHTHALENE AND AIR FOR PREPARING PHTHALIC ANHYDRIDE, ARE PROVIDED. THE LIQUID AROMATIC HYDROCARBON IS ATOMIZED TO FORM DROPLETS HAVING A DIAMETE OF LESS THAN 1 MM AND INJECTED INTO AN OXYGEN-CONTAINING GAS STREAM (12) PREHEATED TO ABOVE THE BOILING POINT OF THE AROMATIC HYDROCARBON. ACCORDING TO THE INVENTION, THE LIQUID AROMATIC HYDROCARBON IS ATOMIZED BY MEANS OF NOZZLES (15) WHICH FORM A HOLLOW CONE (16), PREFERABLY BY MEANS OF SWIRL NOZZLES. THE O-XYLENE/AIR MIXTURE IS ADVANTAGEOUSLY PRODUCED IN A CHAMBER WHICH IS BOUNDED BY SIDE WALLS (18) HEATED TO ABOVE THE BOILING POINT OF THE HYDROCARBON
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公开(公告)号:AT48133T
公开(公告)日:1989-12-15
申请号:AT85111342
申请日:1985-09-07
Applicant: BASF AG
Inventor: BLOCK ULRICH DR
IPC: C07D307/89 , C07C51/573 , C07D307/60 , F28C3/02
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公开(公告)号:DE3566669D1
公开(公告)日:1989-01-12
申请号:DE3566669
申请日:1985-09-07
Applicant: BASF AG
Inventor: BLOCK ULRICH DR , MUFF WOLF , NIXDORF KLAUS , WAGNER JOACHIM
IPC: C07D307/60 , B01J3/00 , C07C51/265 , C07C51/31 , C07D307/89 , F04F5/02
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公开(公告)号:DE3433401A1
公开(公告)日:1986-03-20
申请号:DE3433401
申请日:1984-09-12
Applicant: BASF AG
Inventor: BLOCK ULRICH DR , MUFF WOLF , NIXDORF KLAUS , WAGNER JOACHIM
IPC: C07D307/60 , B01J3/00 , C07C51/265 , C07C51/31 , C07D307/89 , F04F5/02
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公开(公告)号:DE2964430D1
公开(公告)日:1983-02-03
申请号:DE2964430
申请日:1979-10-10
Applicant: BASF AG
Inventor: WOERZ OTTO DR DIPL CHEM , BLOCK ULRICH DR , FISCHER ROMAN DR DIPL CHEM , ROTERMUND GERHARD W DR
IPC: C07C275/04 , C07C273/18 , C07C275/06 , C07C127/15
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公开(公告)号:DE3574377D1
公开(公告)日:1989-12-28
申请号:DE3574377
申请日:1985-09-07
Applicant: BASF AG
Inventor: BLOCK ULRICH DR
IPC: C07D307/89 , C07C51/573 , C07D307/60 , F28C3/02
Abstract: The temperature of the exit gas from the gas washer in the preparation of phthalic anhydride by catalytic oxidation of naphthalene or o-xylene with air is increased by a method in which flue gas from the combustion furnace for residues is mixed with the exit gas before the latter emerges into the atmosphere.
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公开(公告)号:AT39116T
公开(公告)日:1988-12-15
申请号:AT85111341
申请日:1985-09-07
Applicant: BASF AG
Inventor: BLOCK ULRICH DR , MUFF WOLF , NIXDORF KLAUS , WAGNER JOACHIM
IPC: C07D307/60 , B01J3/00 , C07C51/265 , C07C51/31 , C07D307/89 , F04F5/02
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公开(公告)号:DE3433402A1
公开(公告)日:1986-03-20
申请号:DE3433402
申请日:1984-09-12
Applicant: BASF AG
Inventor: BLOCK ULRICH DR
IPC: C07D307/89 , C07C51/573 , C07D307/60 , F28C3/02
Abstract: The temperature of the exit gas from the gas washer in the preparation of phthalic anhydride by catalytic oxidation of naphthalene or o-xylene with air is increased by a method in which flue gas from the combustion furnace for residues is mixed with the exit gas before the latter emerges into the atmosphere.
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公开(公告)号:DE3060960D1
公开(公告)日:1982-11-25
申请号:DE3060960
申请日:1980-04-03
Applicant: BASF AG
Inventor: WOLF DIETER DR , SCHMIDT RUDOLF DR , BLOCK ULRICH DR , SCHOENMAKERS HARTMUT DR , BOTT KASPAR DR , KAIBEL GERD
Abstract: Anhydrous or substantially anhydrous formic acid is obtained by hydrolysis of methyl formate, in a process wherein (a) methyl formate is hydrolyzed, (b) the methanol and excess methyl formate are distilled from the hydrolysis mixture obtained, (c) the bottom product of distillation (b), consisting of formic acid and water, is extracted, in a liquid-liquid extraction, with an extractant which in the main takes up the formic acid, (d) the resulting extract phase, consisting of formic acid, the extractant and a part of the water, is subjected to distillation, (e) the top product obtained from this distillation and consisting of all or part of the water introduced into the distillation, and part of the formic acid, is recycled, as vapor, into the lower part of the distillation column of stage (b), (f) the bottom product of distillation stage (d), consisting of the extractant, with or without part of the water, and the greater part of the formic acid, is separated by distillation into anhydrous or substantially anhydrous formic acid and the extractant, and (g) the extractant leaving stage (f) is recycled to the process.
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