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公开(公告)号:BR7602685A
公开(公告)日:1976-11-09
申请号:BR7602685
申请日:1976-04-30
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J
IPC: B01J23/66 , B01J23/96 , B01J38/48 , B01J38/52 , C07B61/00 , C07D301/10 , C07D303/02 , C07D301/04
Abstract: The efficiency of silver carrier catalysts having reduced activity for the manufacture of ethylene oxide by reacting ethylene with oxygen or air is improved by impregnating the used catalyst with a solution containing cesium and/or rubidium compounds, an aliphatic alcohol and at most 10% by weight of water. After impregnation the alcohol and optionally the water are evaporated. The cesium and/or rubidium content of the impregnating solution and the number of impregnations are adjusted to obtain on the carrier a cesium and/or rubidium concentration of from 1 to 1,000 ppm.
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公开(公告)号:BR8100239A
公开(公告)日:1981-08-04
申请号:BR8100239
申请日:1981-01-16
Applicant: HOECHST AG
Inventor: MAYER S , REBSDAT S , SCHAFFELHOFER I , ALFRANSEDER J
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公开(公告)号:NO761498A
公开(公告)日:1976-11-03
申请号:NO761498
申请日:1976-04-30
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J
CPC classification number: B01J38/485 , B01J23/96 , C07D301/10 , Y02P20/584
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公开(公告)号:SE434804B
公开(公告)日:1984-08-20
申请号:SE7712150
申请日:1977-10-27
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J , RIEDL J
IPC: B01J23/66 , B01J23/96 , B01J31/40 , B01J38/48 , C07B61/00 , C07D301/10 , C07D303/04 , B01J23/54
Abstract: The activity of supported silver catalysts for the direct oxidation of ethylene to ethylene oxide with molecular oxygen or air is improved by applying to the catalyst from 1 to 1,000 ppm, preferably 20 to 500 ppm, of cesium and/or rubidium in two or more than two steps and using the catalyst after each impregnation step again for the production of ethylene oxide by direct oxidation of ethylene with molecular oxygen or air.
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公开(公告)号:BR7707210A
公开(公告)日:1978-07-25
申请号:BR7707210
申请日:1977-10-27
Applicant: HOECHST AG
Inventor: RIEDL J , REBSDAT S , MAYER S , ALFRANSEDER J
IPC: B01J23/66 , B01J23/96 , B01J31/40 , B01J38/48 , C07B61/00 , C07D301/10 , C07D303/04 , B01J31/04 , B01J31/02
Abstract: The activity of supported silver catalysts for the direct oxidation of ethylene to ethylene oxide with molecular oxygen or air is improved by applying to the catalyst from 1 to 1,000 ppm, preferably 20 to 500 ppm, of cesium and/or rubidium in two or more than two steps and using the catalyst after each impregnation step again for the production of ethylene oxide by direct oxidation of ethylene with molecular oxygen or air.
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公开(公告)号:BR8005991A
公开(公告)日:1981-03-31
申请号:BR8005991
申请日:1980-09-19
Applicant: HOECHST AG
Inventor: MAYER S , ALFRANSEDER J , RIEDL J , REBSDAT S , SCHAFFELHOFER I
IPC: B01J23/50 , B01J23/66 , B01J23/68 , B01J23/96 , B01J38/48 , B01J38/66 , C07B61/00 , C07D301/10 , C07D303/04
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公开(公告)号:AU511144B2
公开(公告)日:1980-07-31
申请号:AU2789877
申请日:1977-08-15
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J , RIEDL J
Abstract: The activity of supported silver catalysts used up in the direct oxidation of ethylene with molecular oxygen or air is improved by impregnating the catalyst arranged in a fixed bed with a solution of a caesium and/or rubidium compound in an inert organic solvent, optionally together with up to 40% by weight of water, calculated on the total liquid, as dissolving intermediary, so as to produce a concentration gradient of from 0.3 to 20 parts of caesium and/or rubidium per 1 million parts of catalyst and per meter of fixed bed, counter to the direction of flow of the gas to be reacted. In this manner the activity of the catalyst is considerably improved which results in an increased selectivity of the oxidation of ethylene to ethylene oxide.
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公开(公告)号:BR7705359A
公开(公告)日:1978-06-06
申请号:BR7705359
申请日:1977-08-12
Applicant: HOECHST AG
Inventor: ALFRANSEDER J , MAYER S , REBSDAT S , RIEDL J
Abstract: The activity of supported silver catalysts used up in the direct oxidation of ethylene with molecular oxygen or air is improved by impregnating the catalyst arranged in a fixed bed with a solution of a caesium and/or rubidium compound in an inert organic solvent, optionally together with up to 40% by weight of water, calculated on the total liquid, as dissolving intermediary, so as to produce a concentration gradient of from 0.3 to 20 parts of caesium and/or rubidium per 1 million parts of catalyst and per meter of fixed bed, counter to the direction of flow of the gas to be reacted. In this manner the activity of the catalyst is considerably improved which results in an increased selectivity of the oxidation of ethylene to ethylene oxide.
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公开(公告)号:SE7712150L
公开(公告)日:1978-04-30
申请号:SE7712150
申请日:1977-10-27
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J , RIEDL J
IPC: B01J23/66 , B01J23/96 , B01J31/40 , B01J38/48 , C07B61/00 , C07D301/10 , C07D303/04 , B01J23/54 , C07D
Abstract: The activity of supported silver catalysts for the direct oxidation of ethylene to ethylene oxide with molecular oxygen or air is improved by applying to the catalyst from 1 to 1,000 ppm, preferably 20 to 500 ppm, of cesium and/or rubidium in two or more than two steps and using the catalyst after each impregnation step again for the production of ethylene oxide by direct oxidation of ethylene with molecular oxygen or air.
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公开(公告)号:SE7709149L
公开(公告)日:1978-02-15
申请号:SE7709149
申请日:1977-08-12
Applicant: HOECHST AG
Inventor: REBSDAT S , MAYER S , ALFRANSEDER J , RIEDL J
IPC: B01J23/66 , B01J23/96 , B01J38/48 , B01J38/50 , C07B61/00 , C07D301/10 , B01J23/50 , C07D , C07D303/04
Abstract: The activity of supported silver catalysts used up in the direct oxidation of ethylene with molecular oxygen or air is improved by impregnating the catalyst arranged in a fixed bed with a solution of a caesium and/or rubidium compound in an inert organic solvent, optionally together with up to 40% by weight of water, calculated on the total liquid, as dissolving intermediary, so as to produce a concentration gradient of from 0.3 to 20 parts of caesium and/or rubidium per 1 million parts of catalyst and per meter of fixed bed, counter to the direction of flow of the gas to be reacted. In this manner the activity of the catalyst is considerably improved which results in an increased selectivity of the oxidation of ethylene to ethylene oxide.
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