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US4226782A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of alkylene oxides and catalysts thereof

Assignee: Imperial Chemical Industries Ltd
•
Filing: 1978-05-08
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Granted: 1980-10-07
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Expires: 1998-05-08
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Abstract

Abstract Catalysts for the oxidation of alkenes to alkylene oxides comprise silver on supports having a surface area of 0.05 to 10 m2/g, and at least 16 mu g equivalents per square meter of potassium together with rubidium and/or cesium.

Inventors

  • 👤 Percy Hayden
  • 👤 Richard W. Clayton
  • 👤 Alan F. G. Cope

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 02:47
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/66; B01J35/00; B01J35/60; C; C07; C07D; C07D301/00; C07D301/02; C07D301/03; C07D301/04; C07D301/08; C07D301/10; B01J35/61; B01J35/612; B01J35/63; B01J35/635; B01J35/64; B01J35/653; B01J35/66; B01J35/69

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 118 words
A catalyst for the production of an alkylene oxide by oxidation of the corresponding olefine with oxygen which comprises silver supported on a porous heat resisting support which has a specific surface area in the range 0.05 to 10 m 2 /g as measured by the Brunauer Emmett and Teller method, the catalyst also comprising more than 16 μgram equivalents of potassium per square meter of surface area of the catalyst, the said amount being also more than 1.5×10 -5 gram equivalents per gram of catalyst, together with at least one other alkali metal selected from rubidium and cesium, the said potassium and rubidium and/or cesium being present in a form which is extractable by contact with water.
Claim 2
Dependent Claim 118 words
A catalyst for the production of an alkylene oxide by oxidation of the corresponding olefine with oxygen which comprises silver supported on a porous heat resisting support which has a specific surface area in the range 0.05 to 10 m 2 /g as measured by the Brunauer Emmett and Teller method, the catalyst also comprising more than 16 μgram equivalents of potassium per square meter of surface area of the catalyst, the said amount being also more than 1.5×10 -5 gram equivalents per gram of catalyst, together with at least one other alkali metal selected from rubidium and cesium, the said potassium and rubidium and/or cesium being present in a form which is extractable by contact with water.
Claim 3
Dependent Claim 28 words
A catalyst as claimed in claim 1 in which the porous heat resisting support has a specific surface area in the range 0.3 to 5 m 2 /g.
Claim 4
Dependent Claim 38 words
A catalyst as claimed in claim 1 of which the support has an apparent porosity as measured by the mercury absorption method of 30-80%, and pores of 0.1 to 20 microns as measured by the mercury porosimetry method.
Claim 5
Dependent Claim 35 words
A catalyst as claimed in claim 1 in which the support is composed of an aggregate of alpha-alumina particles which are fused or cemented together and which comprises 3 to 50% by weight of silver.
Claim 6
Dependent Claim 34 words
A catalyst as claimed in claim 1 in which the atomic ratio of potassium to rubidium and cesium taken together in a form which is extractable by contact with water is 1.5:1 to 200:1.
Claim 7
Dependent Claim 52 words
A process of producing a catalyst as claimed in claim 1 which comprises impregnating a suitable support with a solution of a silver compound, introducing compounds of said potassium and said other alkali metal before, during or after the impregnation with the solution of the silver compound, and reducing the silver compound.
Claim 8
Dependent Claim 17 words
A process as claimed in claim 6 in which the solution comprises water and a nitrogen-containing base.
Claim 9
Dependent Claim 28 words
A process for the production of an alkylene oxide by oxidation of the corresponding olefine with oxygen in the presence of a catalyst as claimed in claim 1.

References Cited (Backward Citations)

US3962136A Cited
US4010115A Cited
US3962136B1 Cited
US4007135A Cited
US4033903A Cited
US4066575A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-10-07 1984-04-07 1984-10-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-10-07 1988-04-07 1988-10-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-10-07 1992-04-07 1992-10-07 $7700.00 Window Closed / Lapsed

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