Ethylene oxide catalyst and process

• US 5,663,385 A
• Filed: 05/09/1996
• Issued: 09/02/1997
• Est. Priority Date: 11/01/1994
• Status: Expired due to Fees

• Current Assignee: Shell Oil Company (Shell Plc)
• Original Assignee: Shell Oil Company (Shell Plc)
• Inventors: Kemp, Richard Alan
• Primary Examiner(s): Caldarola, Glenn A.
• Assistant Examiner(s): Yildirim, Bekir L.
• Application Number:
  US08/645,011
• Time in Patent Office: 481 Days
• Field of Search: 549/536, 549/534, 502/347
• US Class Current: 549/536
• CPC Class Codes: B01J 23/688 with manganese, technetium or rhenium
• CPC Class Codes: B01J 27/1817 with copper, silver or gold
• CPC Class Codes: B01J 27/187 with manganese, technetium or rhenium
• CPC Class Codes: C07D 301/10 with catalysts containing silver or gold
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

This invention relates to an ethylene oxide catalyst having improved initial selectivity which catalyst comprises silver, a promoting amount of alkali metal, a promoting amount of rhenium and a promoting amount of rhenium-co-promoter selected from phosphorus, boron and mixtures thereof, supported on a porous refractory support.

Claims

1. In a process for the production of ethylene oxide wherein ethylene is contacted in the vapor phase with an oxygen-containing gas at ethylene oxide forming conditions at a temperature in the range of from about 180°

C. to about 330°

C. in the presence of a silver metal-containing catalyst, the improvement which comprises using a catalyst comprising a catalytically effective amount of silver, a promoting amount of alkali metal, a promoting amount of rhenium and a rhenium co-promoter selected from phosphorus, boron and mixtures thereof supported on a suitable support having a surface area in the range of from about 0.05m² /g to about 10 m² /g.

2. In a process for the production of ethylene oxide wherein ethylene is contacted in the vapor phase with an oxygen-containing gas at ethylene oxide forming conditions at a temperature in the range of from about 180°

C. to about 330°

C. in the presence of a silver metal-containing catalyst, the improvement which comprises using a catalyst comprising from about 1 percent by weight to about 25 percent by weight of the total catalyst of the silver compound(s), expressed as the metal, from about 10 parts per million to about 3000 parts per million by weight of alkali metal compound(s), expressed as the metal, per million parts by weight of the total catalyst, from about 0.1 micromoles to about 10 micromoles per gram of total catalyst of rhenium compound(s), expressed as the metal, and from about 0.1 micromoles to about 10 micromoles per gram of total catalyst of rhenium co-promoter compound(s) wherein the rhenium co-promoter compound is selected from compounds of phosphorus, boron and mixtures thereof, expressed as the element, to provide the catalyst with a catalytically effective amount of silver, a promoting amount of alkali metal, a promoting amount of rhenium and a promoting amount of rhenium co-promoter.