Method of starting-up a process of producing an alkylene oxide using a high-efficiency catalyst

• US 8,987,483 B2
• Filed: 12/01/2011
• Issued: 03/24/2015
• Est. Priority Date: 12/15/2010
• Status: Active Grant

• Current Assignee: Dow Technology Investments LLC (Dow, Inc.)
• Original Assignee: Dow Technology Investments LLC (Dow, Inc.)
• Inventors: Basrur, Arun G., Soo, Hwaili, Hinman, Paul V., Tupe, Ravindra R.
• Primary Examiner(s): Oh, T. Victor
• Application Number:
  US13/994,233
• Publication Number:
  US 20140024846A1
• Time in Patent Office: 1,209 Days
• Field of Search: 549/536
• US Class Current: 549/536
• CPC Class Codes: B01J 23/688 with manganese, technetium or rhenium
• CPC Class Codes: C07D 301/10 with catalysts containing silver or gold
• CPC Class Codes: Y02P 20/582 Recycling of unreacted starting or intermediate materials

Abstract

A method for starting-up a high efficiency alkylene oxide catalyst is described. A feed gas comprising an alkylene, oxygen, and at least one organic chloride is introduced to the catalyst. The molar ratio of oxygen to alkylene, reaction temperature, and overall chloriding effectiveness are adjusted to specified ranges of values within a specified catalyst aging period.

Claims

1. A method for starting-up an alkylene oxide production process, the alkylene oxide production process comprising reacting a feed gas comprising an alkylene, oxygen, and at least one organic chloride over a high efficiency silver catalyst to yield a reaction product comprising the alkylene oxide, the start-up method comprising:

providing a feed gas comprising the alkylene, oxygen, and the at least one organic chloride, wherein the feed gas has an overall chloriding effectiveness represented by the formula;

2. The method of claim 1, further comprising selecting a target alkylene oxide concentration in the reaction product and maintaining the molar ratio of oxygen to alkylene of at least 0.2 no longer than until the start-up concentration of the alkylene oxide in the reaction product is equal to the target concentration of the alkylene oxide in the reaction product.

3. The method claim 2, wherein the step of maintaining the molar ratio of oxygen to the alkylene in the feed gas of at least 0.2 is conducted no longer than until the efficiency of the process to the alkylene oxide is at least 85%.

4. The method of claim 2, wherein the step of maintaining the molar ratio of oxygen to the alkylene in the feed gas of at least 0.2 is conducted no longer than until the start-up concentration of the alkylene oxide in the reaction product is at least 1.5 mole %.

5. The method of claim 1, wherein the step of adjusting both the reaction temperature and the overall chloriding effectiveness comprises adjusting at least one of the reaction temperature and Z* according to the following relationship:

Z*=(T_rx−

T_o)/S_o

wherein, T_rx is the reactor coolant inlet temperature in °

C.,

T_o is the temperature-axis intercept calculated by extrapolating a plot of Z* versus T_rx to Z*=0, and

S_o is a slope relating the change in inlet coolant temperature to the corresponding change in Z*.

6. The method of claim 1, wherein within a catalyst aging period of no greater than 0.02 kT alkylene oxide/m³ catalyst after the reactor is first on-stream, the reaction temperature is from 225°

C. to 235°

C.

7. The method of claim 1, wherein within no more than 5 hours after the reactor is first on stream, the molar ratio of oxygen to the alkylene in the feed gas is at least 0.15.

8. The method of claim 1, wherein within a catalyst aging period of no greater than 0.02 kT alkylene oxide/m³ catalyst after the reactor is first on-stream, the molar ratio of oxygen to the alkylene in the feed gas is no more than 0.35.

9. A method for producing an alkylene oxide by reacting an alkylene, oxygen, and at least one organic chloride over a high efficiency silver catalyst, the method comprising:

reacting a feed gas comprising the alkylene, oxygen, and at least one organic chloride over the high-efficiency silver catalyst at a reaction temperature and an overall chloriding effectiveness to yield a reaction product comprising the alkylene oxide such that the process has a molar ratio of oxygen to the alkylene in the feed gas and a first efficiency to the alkylene oxide, the first efficiency to the alkylene oxide being less than a target efficiency to the alkylene oxide;

adjusting at least one process parameter such that the efficiency of the process to the alkylene oxide increases from the first efficiency to a second efficiency, wherein the at least one process parameter is selected from the group consisting of the molar ratio of oxygen to the alkylene in the feed gas, reactor temperature, and overall chloriding effectiveness, following the adjusting step the molar ratio of oxygen to the alkylene in the feed gas is at least 0.2, the reaction temperature is from 215°

C. to 240°

C., the overall chloriding effectiveness is represented as Z* and is from 1.0 to 5.0, and Z* is represented as follows;

10. The method of claim 9, wherein the at least one process parameter includes reaction temperature, and the step of adjusting the reaction temperature comprises adjusting the reaction temperature from a value outside the range of 225°

C. to 235°

C. to a value inside the range of 225°

C. to 235°

C.

11. The method of claim 9, wherein the at least one process parameter includes the molar ratio of oxygen to alkylene in the feed gas, and the step of adjusting the molar ratio of oxygen to alkylene in the feed gas comprises adjusting the molar ratio from a first value of less than 0.2 to a second value of at least 0.2.

12. The method of claim 9, wherein the second efficiency to the alkylene oxide is at least 85%.

13. The method of claim 9, wherein following the adjusting step the molar ratio of oxygen to the alkylene in the feed gas is no more than 0.35.

14. The method of claim 9, wherein the at least one process parameter includes Z*, and the step of adjusting Z* comprises adjusting Z* from a first value outside the range of from 1.0 to 5.0 to a second value inside the range of from 1.0 to 5.0.

15. The method of claim 9, wherein the at least one process parameter includes the molar ratio of oxygen to alkylene in the feed gas, reaction temperature, and Z*, the step of adjusting the molar ratio of oxygen to alkylene in the feed gas comprises adjusting the molar ratio from a first value of less than 0.2 to a second value of at least 0.2, the step of adjusting the reaction temperature comprises adjusting the reaction temperature from a first value outside the range of from 215°

C. to 240°

C. to a second value inside the range of from 215°

C. to 240°

C., and the step of adjusting Z* comprises adjusting Z* from a first value outside the range of from 1.0 to 5.0 to a second value inside the range of from 1.0 to 5.0.