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公开(公告)号:SE7503559L
公开(公告)日:1975-10-02
申请号:SE7503559
申请日:1975-03-26
Applicant: HOECHST AG
Inventor: LOHMAR E , OHORODNIK A , GEHRMANN K , STUTZKE P , STAENDEKE H
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公开(公告)号:DK135275A
公开(公告)日:1975-10-02
申请号:DK135275
申请日:1975-03-26
Applicant: HOECHST AG
Inventor: LOHMAR E , OHORODNIK A , GEHRMANN K , STUTZKE P , STAENDEKE H
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公开(公告)号:DK141547C
公开(公告)日:1980-11-03
申请号:DK526671
申请日:1971-10-28
Applicant: HOECHST AG
Inventor: OHORODNIK A , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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公开(公告)号:NL176232B
公开(公告)日:1984-10-16
申请号:NL7114863
申请日:1971-10-28
Applicant: HOECHST AG
Inventor: OHORODNIK A , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377 , B01J8/08
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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公开(公告)号:ZA7603944B
公开(公告)日:1977-06-29
申请号:ZA7603944
申请日:1976-07-02
Applicant: HOECHST AG
Inventor: LOHMAR E , GEHRMANN K , OHORODNIK A , STUTZKE P
CPC classification number: C07F9/34
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公开(公告)号:CH563186A5
公开(公告)日:1975-06-30
申请号:CH1583071
申请日:1971-10-29
Applicant: HOECHST AG
Inventor: OHORODNIK A , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377 , B01J8/08
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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公开(公告)号:DK141547B
公开(公告)日:1980-04-21
申请号:DK526671
申请日:1971-10-28
Applicant: HOECHST AG
Inventor: OHORODNIK , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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公开(公告)号:DE2053115C3
公开(公告)日:1978-08-31
申请号:DE2053115
申请日:1970-10-29
Applicant: HOECHST AG, 6000 FRANKFURT
Inventor: OHORODNIK A , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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公开(公告)号:ZA763944B
公开(公告)日:1977-06-29
申请号:ZA763944
申请日:1976-07-02
Applicant: HOECHST AG
Inventor: LOHMAR E , GEHRMANN K , OHORODNIK A , STUTZKE P
Abstract: Beta-halogenoformyl-ethyl phosphinic acid halides of the general formula:
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公开(公告)号:NL176232C
公开(公告)日:1985-03-18
申请号:NL7114863
申请日:1971-10-28
Applicant: HOECHST AG
Inventor: OHORODNIK A , SENNEWALD K , HUNDECK J , STUTZKE P
IPC: B01J8/00 , B01J8/18 , B01J8/22 , C07C51/377 , B01J8/08
Abstract: 1363245 Liquid phase catalytic process, separating solids from liquid KNAPSACK AG 4 Oct 1971 [29 Oct 1970] 46060/71 Headings B1D and B1F In catalyst/liquid separator 7, liquid product is drawn off through valve 11 at a rate such that the upward rate of flow of liquid in separator 7 is less than the rate of sedimentation of catalyst in the separator. Circulation of reaction mixture is effected by the gas-lift effect of gas from line 9 and pump 3. The hydrogenative dehalogenation of dichloracetic acid to produce monochloracetic acid is described using a palladium catalyst on a silica carrier.
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