Epoxidation methods

Patent metadata

Field	Value
Publication number	US-9458121-B2
Application number	US-201614992586-A
Country	US
Kind code	B2
Filing date	Jan 11, 2016
Priority date	Jun 6, 2011
Publication date	Oct 4, 2016
Grant date	Oct 4, 2016

Abstract

A method for the epoxidation of alkylenes is provided. The method makes use of an epoxidation catalyst comprising a support, silver, manganese and greater than 35 ppm sodium. The catalyst is produced by a method comprising impregnating the support with manganese prior to impregnating the support with sodium and impregnating the support with silver prior to, at the same time as, or after impregnation with manganese. A method for using the alkylene oxides for the production of 1,2-diols, 1,2-carbonates, 1,2-diol ethers is also provided.

First claim

We claim:

1. A method for the epoxidation of one or more alkylenes comprising contacting one or more feed streams comprising an oxygen source and an alkylene in the presence of an epoxidation catalyst, wherein the epoxidation catalyst comprises a support, silver, manganese and greater than 35 ppm sodium, and is prepared by a method comprising:
Impregnating the support with manganese prior to impregnating the support with sodium; and
Impregnating the support with silver prior to, at the same time as or after impregnation with manganese.

2. The method of claim 1 , carried out in the gas phase over a packed catalyst bed wherein the gas hourly space velocity in the start-up phase is from 2000 to 10000 per hour.

3. The method of claim 1 , wherein the alkylene comprises 1,9-decadiene, 1,3-butadiene, 2-butene, isobutene, 1-butene, propylene, ethylene, or combinations of these.

4. The method of claim 1 , wherein the one or more feed streams further comprises one or more gas phase promoters selected from the group consisting of methyl chloride, ethyl chloride, ethylene dichloride, ethylene dibromide, vinyl chloride, and any combination of these.

5. The method of claim 1 , wherein the one or more feed streams further comprises carbon dioxide in a concentration of at most 3 mole percent, based on the total reaction mixture.

6. The method of claim 1 , wherein the concentration of oxygen within the oxygen source is decreased by up to 3 mole percent during the epoxidation process.

7. The method of claim 5 , wherein the concentration of carbon dioxide is increased during the epoxidation process by at least 0.5 mole percent during the epoxidation process.

8. A method for the epoxidation of one or more alkylenes comprising contacting one or more feed streams comprising an oxygen source and an alkylene in the presence of an epoxidation catalyst, wherein the epoxidation catalyst comprises a support, silver, manganese and greater than 35 ppm sodium, and is prepared by a method comprising:
Impregnating the support with manganese separately from sodium and exposing the catalyst in between impregnations to an elevated temperature not exceeding 600° C.

9. The method of claim 8 , carried out in the gas phase over a packed catalyst bed wherein the gas hourly space velocity in the start-up phase is from 2000 to 10000 per hour.

10. The method of claim 8 , wherein the alkylene comprises 1,9-decadiene, 1,3-butadiene, 2-butene, isobutene, 1-butene, propylene, ethylene, or combinations of these.

11. The method of claim 8 , wherein the one or more feed streams further comprises one or more gas phase promoters selected from the group consisting of methyl chloride, ethyl chloride, ethylene dichloride, ethylene dibromide, vinyl chloride, and any combination of these.

12. The method of claim 8 , wherein the one or more feed streams further comprises carbon dioxide in a concentration of at most 3 mole percent, based on the total reaction mixture.

13. The method of claim 12 , wherein the concentration of carbon dioxide is increased during the epoxidation process by at least 0.5 mole percent during the epoxidation process.

14. The method of claim 1 , further comprising reacting the alkylene oxide with water, alcohol, ammonia and/or carbon dioxide to provide a 1,2-diol, 1,2-diol ether, a 1,2-carbonate, or alkanolamine.

15. The method of claim 14 , wherein the alkylene oxide is reacted with water and/or alcohol, optionally in the presence of an acidic or basic catalyst, to produce one or more 1,2-diols or 1,2-diol ethers.

16. The method of claim 14 , wherein the alkylene oxide is reacted with ammonia to produce one or more alkanolamines.

17. The method of claim 14 , wherein the the alkylene oxide is reacted with carbon dioxide to provide a 1,2-carbonate.

18. The method of claim 8 , further comprising reacting the alkylene oxide with water, alcohol, ammonia and/or carbon dioxide to provide a 1,2-diol, 1,2-diol ether, a 1,2-carbonate, or alkanolamine.

19. The method of claim 18 , wherein the alkylene oxide is reacted with water and/or alcohol, optionally in the presence of an acidic or basic catalyst, to produce one or more 1,2-diols or 1,2-diol ethers.

20. The method of claim 18 , wherein the alkylene oxide is reacted with ammonia to produce one or more alkanolamines, or, reacting the alkylene oxide with carbon dioxide to provide a 1,2-carbonate.

Assignees

• Dow Technology Investments Llc

Inventors

• Gopal Srikant
• Murthy Lakshmi N Vutukuru
• Basrur Arun G

Classifications

• C07C213/02

  by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups · CPC title

• B01J23/688

  with manganese, technetium or rhenium · CPC title

• B01J2523/18

  Silver · CPC title

• C07C41/02

  from oxiranes · CPC title

• B01J27/055

  with alkali metals, copper, gold or silver · CPC title