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公开(公告)号:DE1151506B
公开(公告)日:1963-07-18
申请号:DEB0061419
申请日:1961-02-24
Applicant: BASF AG
Inventor: CRAUBNER DR HANS , HRUBESCH DR ADOLF , BURGER DR HEINZ , KRZIKALLA DR REINHARD
IPC: C07D233/56 , C09K15/30
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公开(公告)号:DE1138934B
公开(公告)日:1962-10-31
申请号:DEB0056153
申请日:1960-01-07
Applicant: BASF AG
Inventor: CRAUBNER DR HANS , HRUBESCH DR ADOLF
IPC: C08F283/00 , C08F283/04
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公开(公告)号:DE1133547B
公开(公告)日:1962-07-19
申请号:DEB0058505
申请日:1960-07-07
Applicant: BASF AG
Inventor: JOST DR KONRAD , GEHM DR ROBERT , HRUBESCH DR ADOLF
IPC: C08K5/30
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公开(公告)号:DE1111391B
公开(公告)日:1961-07-20
申请号:DEB0056152
申请日:1960-01-07
Applicant: BASF AG
Inventor: CRAUBNER DR HANS , HRUBESCH DR ADOLF
IPC: C08F8/30 , C08F291/12
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公开(公告)号:DE1088049B
公开(公告)日:1960-09-01
申请号:DEB0039640
申请日:1956-03-24
Applicant: BASF AG
Inventor: HRUBESCH DR ADOLF
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公开(公告)号:DE1026025B
公开(公告)日:1958-03-13
申请号:DEB0041628
申请日:1956-09-04
Applicant: BASF AG
Inventor: HRUBESCH DR ADOLF , FRANKE DR WALTER
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公开(公告)号:DE1004318B
公开(公告)日:1957-03-14
申请号:DEB0038745
申请日:1956-01-17
Applicant: BASF AG
Inventor: HRUBESCH DR ADOLF , FRANKE DR WALTER
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公开(公告)号:DE1002329B
公开(公告)日:1957-02-14
申请号:DEB0030597
申请日:1954-04-14
Applicant: BASF AG
Inventor: HRUBESCH DR ADOLF
IPC: C23F11/10
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公开(公告)号:DE831755C
公开(公告)日:1952-02-18
申请号:DEB0003047
申请日:1950-04-15
Applicant: BASF AG
Inventor: HRUBESCH DR ADOLF , SCHLICHTING DR OTTO
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公开(公告)号:DE1568094A1
公开(公告)日:1970-05-06
申请号:DE1568094
申请日:1966-03-24
Applicant: BASF AG
Inventor: SUTER DR HUBERT , NOHE DR HEINZ , BECK DR FRITZ , HRUBESCH DR ADOLF
Abstract: 1,176,036. Cyclohexadiene dicarboxylic acids. BADISCHE ANILIN- & SODA-FABRIK A.G. 23 March, 1967 [24 March, 1966], No. 13721/67. Heading C2C. [Also in Division C7] 3,5 or 2,5-Cyclohexadiene-1,2 or 1,4-dicarboxylic acid is produced by electrochemical hydrogenation of o- and/or tere-phthalic acid in aqueous H 2 SO 4 at 70-100 C. with a current density of 1-40 amp./sq. dm. on a cathode of Cd, Sn, Bi, Tl, or an alloy of at least two of the metals Pb, Hg, Ag, Cd, Sn, Tl and Bi; the cathode metal or alloy may be amalgamated. The phthalic acid may be dispersed in a concentration of 2-8% in aqueous H 2 SO 4 of concentration 2-50% by weight. The hydrogenation cell may be a heated or cooled doublewalled tube provided with a cylindrical cathode on or as its inner wall surrounding a cylindrical porous clay diaphragm and a water-cooled lead pipe anode; alternatively, the anode may be of Pb, Pt, PbO 2 , graphite or SiC. The catholyte may be continuously fed to the cell by a metering pump; withdrawn catholyte may be returned to the cell after crystallizing out the product and adding phthalic acid. Aqueous H 2 SO 4 may form the anolyte.
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