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公开(公告)号:CA1157479A
公开(公告)日:1983-11-22
申请号:CA385522
申请日:1981-09-09
Applicant: BASF AG
Inventor: MUELLER FRANZ-JOSEF , STEINER WOLFGANG , ROSS KARL-HEINZ , KRATZER OTTO
Abstract: O.Z. 0050/034690 of the disclosure: A process for the preparation of methyl formate by reacting methanol and carbon monoxide in the presence of an alkali metal alcoholate or alkaline earth metal alcoholate at from 30 to 150.degree.C and from 50 to 300 bar, wherein a nonionic complexing agent is used to bind the alkali metal cations or alkaline earth metal cations.
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公开(公告)号:NO820506L
公开(公告)日:1982-08-20
申请号:NO820506
申请日:1982-02-18
Applicant: BASF AG
Inventor: BOTT KASPAR , KAIBEL GERD , HOFFMANN HERWIG , IRNICH RUDOLF , KRATZER OTTO
IPC: C07C231/02 , C07C20060101 , C07C67/00 , C07C231/00 , C07C233/03 , C07C
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公开(公告)号:NO820506A
公开(公告)日:1982-08-20
申请号:NO820506
申请日:1982-02-18
Applicant: BASF AG
Inventor: BOTT KASPAR , KAIBEL GERD , HOFFMANN HERWIG , IRNICH RUDOLF , KRATZER OTTO
IPC: C07C231/02 , C07C20060101 , C07C67/00 , C07C231/00 , C07C233/03 , C07C
CPC classification number: C07C231/02 , C07C233/03
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公开(公告)号:NO794080L
公开(公告)日:1980-06-17
申请号:NO794080
申请日:1979-12-13
Applicant: BASF AG
Inventor: BOTT KASPAR , KAIBEL GERD , HOFFMANN HERWIG , KRATZER OTTO , IRNICH RUDOLF
Abstract: A process for the production of anhydrous or substantially anhydrous formic acid by hydrolysis of methyl formate which is carried out in a column having an upper fractionating section, a middle hydrolysis section and a lower extraction section and in which (a) the hydrolysis is carried out in the middle section of the columm, with water and methyl formate in countercurrent, (b) the resulting formic acid is extracted, in the lower section of the column, by means of a carboxylic acid amide which is fed into the lower end of the middle section of the column, (c) the extract phase, consisting in the main of formic acid and the carboxylic acid amide, is distillatively dehydrated, or substantially dehydrated, in the lower section of the column, (d) the methanol and uncovered methyl formate are removed by fractional distillation in the upper section of the column and (e) the pure formic acid or concentrated aqueous formic acid is distilled from the anhydrous or substantially anhydrous extract phase in a second column, leaving the carboxylic acid amide.
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公开(公告)号:MY120022A
公开(公告)日:2005-08-30
申请号:MYPI9800882
申请日:1998-02-27
Applicant: BASF AG
Inventor: ULRICH BERNHARD , HEFELE GERHARD , KRATZER OTTO , SCHEIDMEIR WALTER
IPC: B01J23/04 , B01J23/22 , B01J37/02 , C07C51/255 , C07C51/265 , C07C51/31 , C07D307/89
Abstract: IN A PROCESS FOR PREPARING PHTHALIC ANHYDRIDE BY CATALYTIC GAS-PHASE OXIDATION OF O-XYLENE OR NAPHTHALENE OR O-XYLENE/NAPHTHALENE MIXTURES WITH A GAS COMPRISING MOLECULAR OXYGEN OVER A COATED CATALYST COMPRISING AN INERT, NONPOROUS SUPPORT MATERIAL ON WHICH A CATALYTICALLY ACTIVE COMPOSITION COMPRISING TITANIUM DIOXIDE AND VANADIUM PENTOXIDE IS APPLIED IN LAYER FROM, A CATALYST WHOSE CATALYTICALLY ACTIVE COMPOSITION COMPRISES FROM 3 TO 6% BY WEIGHT OF VANADIUM PENTOXIDE, CALCULATED AS V2O3, FROM 0.3 TO 0.5% BY WEIGHT OF A CESIUM COMPOUND, CALCULATED AS CS, AND THE REMAINDER TO 100% BY WEIGHT OF TITANIUM DIOXIDE IN THE ANATASE MODIFICATION IS USED IN THE PRESENCE OR ABSENCE OF A COATED CATALYST, DIFFERING THEREFROM , FOR THE CATALYTIC GAS-PHASE OXIDATION OF O-XYLENE OR NAPHTHALENE OR O-XYLENE/NAPHTHALENE MIXTURES AND, IN THE PRESENCE OF SUCH A SECOND CATALYST, THE LATTER IS USED IN A COMBINED BED WITH THE CATALYST OF THE ABOVE COMPOSITION IN THE REACTOR.
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公开(公告)号:ES2198051T3
公开(公告)日:2004-01-16
申请号:ES98912298
申请日:1998-02-12
Applicant: BASF AG
Inventor: HEFELE GERHARD , KRATZER OTTO , SCHEIDMEIR WALTER , ULRICH BERNHARD
IPC: B01J23/04 , B01J23/22 , B01J37/02 , C07C51/255 , C07C51/265 , C07C51/31 , C07D307/89
Abstract: In a process for preparing phthalic anhydride by catalytic gas-phase oxidation of o-xylene or naphthalene or o-xylene/naphthalene mixtures with a gas comprising molecular oxygen over a coated catalyst comprising an inert, nonporous support material on which a catalytically active composition comprising titanium dioxide and vanadium pentoxide is applied in layer form, a catalyst whose catalytically active composition comprises from 3 to 6% by weight of vanadium pentoxide, calculated as V2O5, from 0.3 to 0.5% by weight of a cesium compound, calculated as Cs, and the remainder to 100% by weight of titanium dioxide in the anatase modification is used in the presence or absence of a coated catalyst, differing therefrom, for the catalytic gas-phase oxidation of o-xylene or naphthalene or o-xylene/naphthalene mixtures and, in the presence of such a second catalyst, the latter is used in a combined bed with the catalyst of the above composition in the reactor.
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公开(公告)号:DE59808067D1
公开(公告)日:2003-05-28
申请号:DE59808067
申请日:1998-02-12
Applicant: BASF AG
Inventor: HEFELE GERHARD , KRATZER OTTO , SCHEIDMEIR WALTER , ULRICH BERNHARD
IPC: B01J23/04 , B01J23/22 , B01J37/02 , C07C51/255 , C07C51/265 , C07C51/31 , C07D307/89
Abstract: In a process for preparing phthalic anhydride by catalytic gas-phase oxidation of o-xylene or naphthalene or o-xylene/naphthalene mixtures with a gas comprising molecular oxygen over a coated catalyst comprising an inert, nonporous support material on which a catalytically active composition comprising titanium dioxide and vanadium pentoxide is applied in layer form, a catalyst whose catalytically active composition comprises from 3 to 6% by weight of vanadium pentoxide, calculated as V2O5, from 0.3 to 0.5% by weight of a cesium compound, calculated as Cs, and the remainder to 100% by weight of titanium dioxide in the anatase modification is used in the presence or absence of a coated catalyst, differing therefrom, for the catalytic gas-phase oxidation of o-xylene or naphthalene or o-xylene/naphthalene mixtures and, in the presence of such a second catalyst, the latter is used in a combined bed with the catalyst of the above composition in the reactor.
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公开(公告)号:CA1266682A
公开(公告)日:1990-03-13
申请号:CA513909
申请日:1986-07-16
Applicant: BASF AG
Inventor: HOELDERICH WOLFGANG , MERGER FRANZ , KRATZER OTTO , SCHEIDMEIR WALTER
IPC: C07C49/04 , B01J29/00 , C07B61/00 , C07C1/00 , C07C1/24 , C07C11/18 , C07C45/00 , C07C45/50 , C07C45/51 , C07C45/54 , C07C67/00 , C07C1/253
Abstract: Methyl isopropyl ketone and isoprene are prepared by converting a pivalaldehyde containing reaction mixture over a zeolite catalyst at elevated temperatures, the said reaction mixture being obtained by hydroformylation of isobutene or of an isobutene-containing C4 cut.
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公开(公告)号:FI77019C
公开(公告)日:1989-01-10
申请号:FI820118
申请日:1982-01-14
Applicant: BASF AG
Inventor: BOTT KASPAR , KAIBEL GERD , HOFFMANN HERWIG , IRNICH RUDOLF , KRATZER OTTO
IPC: C07C231/02 , C07C20060101 , C07C67/00 , C07C231/00 , C07C233/03 , C07C103/12 , C07C102/06
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公开(公告)号:NO156939C
公开(公告)日:1987-12-23
申请号:NO820506
申请日:1982-02-18
Applicant: BASF AG
Inventor: BOTT KASPAR , KAIBEL GERD , HOFFMANN HERWIG , IRNICH RUDOLF , KRATZER OTTO
IPC: C07C231/02 , C07C20060101 , C07C67/00 , C07C231/00 , C07C233/03 , C07C103/127 , C07C102/06
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