Process for manufacturing ethylene oxide using scaled selectivity values

Patent metadata

Field	Value
Publication number	US-2017362193-A1
Application number	US-201515540076-A
Country	US
Kind code	A1
Filing date	Sep 30, 2015
Priority date	Dec 30, 2014
Publication date	Dec 21, 2017
Grant date	—

Abstract

Disclosed herein are methods of using scaled selectivities to assist in determining whether changes to the value of a target ethylene oxide production parameter—such as ethylene oxide production rate—used in the process of epoxidizing ethylene with a high-selectivity catalyst, have caused the process to move away from optimal operation. If the deviation from optimal operation has not worsened, it is generally unnecessary to perform a full optimization study even if the value of a target ethylene oxide production parameter has changed, which reduces or eliminates process disturbances caused by carrying out such studies. Methods are also disclosed which use both scaled selectivities and scaled reaction temperatures. If scaled selectivities reveal that a change in the value of a target ethylene oxide production parameter has moved the process away from optimal operation, scaled reaction temperatures can, under certain conditions, provide an indication of the directions in which the reaction temperature and/or overall catalyst chloriding effectiveness should be changed to move toward optimal operation. If a change in the value of a target ethylene oxide production parameter has improved the scaled selectivity, the scaled reaction temperature may also be used to guide further adjustments which may further improve scaled selectivity.

First claim

1 . A method of operating a process for producing ethylene oxide by reacting a feed gas comprising ethylene, oxygen, and at least one organic chloride over a high selectivity, silver-based catalyst comprising rhenium, the method comprising the steps of:
operating the process at a first value of a reaction temperature, a first value of an overall catalyst chloriding effectiveness, and a first set of values for a set of reference operating conditions, the set of reference operating conditions comprising a plurality of reference reaction parameters, to yield a first value of a target ethylene oxide production parameter and a first actual selectivity value; operating the process at a second value of the reaction temperature, a second value of the overall catalyst chloriding effectiveness, and a second set of values for the set of reference operating conditions, to yield a second value of the target ethylene oxide production parameter and a second actual selectivity value; calculating a scaled second selectivity value from the second actual selectivity, a value in the second set of values of at least one of the reference operating conditions in the set of reference operating conditions, and a reference value of the at least one of the reference operating conditions in the set of reference operating conditions; determining that an adjustment is required to at least one of the reaction temperature and the overall catalyst chloriding effectiveness based on the scaled second selectivity value and the first actual selectivity value, and subsequently adjusting at least one of the reaction temperature to a third reaction temperature value and the overall catalyst chloriding effectiveness to a third overall catalyst chloriding effectiveness value, such that the scaled selectivity increases.

2 . The method of claim 1 , wherein the step of calculating a scaled second selectivity value from the second actual selectivity, the value in the second set of values of at least one of the reference operating conditions in the set of reference operating conditions, and a reference value of the at least one of the reference operating conditions in the set of reference operating conditions comprises calculating the scaled second selectivity value using a selectivity scaling relationship selected from the group consisting of a linear relationship and a non-linear relationship.

3 . The method of claim 1 , wherein the step of determining that an adjustment is required to at least one of the reaction temperature and the overall catalyst chloriding effectiveness comprises comparing an absolute value of a difference between the scaled second selectivity value and the first actual selectivity value to a pre-determined value.

4 . The method of claim 1 , further comprising the step of calculating a scaled first selectivity value from the first actual selectivity value, a value in the first set of values of the at least one of the reference operating conditions in the set of reference operating conditions, and the reference value of the at least one of the reference operating conditions in the set of reference operating conditions, wherein the step of determining that an adjustment is required to at least one of the reaction temperature and the overall catalyst chloriding effectiveness is based on the scaled second selectivity value and the scaled first selectivity value.

5 . The method of claim 1 , wherein each reference operating condition in the set of reference operating conditions has a reference value, and each reference value for each reference operating condition in the set of reference operating conditions differs from the corresponding value in the first set of values for the set of reference operating conditions and the corresponding value in the second set of values for the set of reference operating conditions.

6 . The method of claim 1 , wherein the set of reference operating conditions includes an ethylene oxide production parameter selected from the group consisting of ethylene oxide concentration, ethylene oxide yield, ethylene oxide production rate, ethylene oxide production rate/catalyst volume, ethylene conversion, and oxygen conversion.

7 . The method of claim 6 , wherein the set of reference operating conditions further includes at least one selected from the group consisting of an oxygen concentration, an ethylene concentration, a carbon dioxide concentration, a reactor pressure, and a gas hourly space velocity.

8 . The method of claim 1 , wherein the step of adjusting at least one of the reaction temperature to a third reaction temperature value and the overall catalyst chloriding effectiveness to a third overall catalyst chloriding effectiveness value comprises adjusting the at least one of the reaction temperature to a third reaction temperature value and the overall catalyst chloriding effectiveness to a third overall catalyst chloriding effectiveness value until the second scaled selectivity value is observed at the second value of the target ethylene oxide production parameter.

9 . The method of claim 4 , wherein the at least one of the reference operating conditions in the set of reference operating conditions is a first at least one of the reference operating conditions in the set of reference operating conditions, the method further comprising the steps of:
calculating a scaled second reaction temperature value from the second value of the reaction temperature, a value in the second set of values of a second at least one of the reference operating conditions in the set of reference operating conditions, and a reference value of the second at least one of the reference operating conditions in the set of reference operating conditions, wherein the step of adjusting at least one of the reaction temperature to a third reaction temperature value and the overall catalyst chloriding effectiveness to a third overall catalyst chloriding effectiveness value is further based on the scaled second reaction temperature and the first value of the reaction temperature.

10 . The method of claim 9 , wherein the step of calculating a scaled second reaction temperature value from the second value of the reaction temperature, the value in the second set of values of the second at least one of the reference operating conditions in the set of reference operating conditions, and a reference value of the second at least one of the reference operating conditions in the set of reference operating conditions comprises calculating the scaled second reaction temperature value using a reaction temperature scaling relationship selected from the group consisting of a linear relationship and a non-linear relationship.

11 . The method of claim 9 , further comprising the step of calculating a scaled first reaction temperature value from the first value of the reaction temperature, a value in the first set of values of the second at least one of the reference operating conditions in the set of reference operating conditions, and a reference value of the second at least one of the reference operating conditions in the set of reference operating conditions, wherein the step of adjusting at least one of the reaction temperature to a third reaction temperature value and the overall catalyst chloriding effectiveness to a third overall catalyst chloriding effectiveness value is further based on the scaled second reaction temperature and the scaled first reaction temperature value.

12 . The method of claim 11 , wherein the step of operating the process at a first value of the reaction temperature, a first value of the overall catalyst chloriding effectiveness, and a first set of values for the set of reference operating conditions occ

Assignees

• Dow Technology Investments Llc

Inventors

• Phillips Ailene Gardner

Classifications

• C07D301/10 Primary

  with catalysts containing silver or gold · CPC title

• B01J23/688

  with manganese, technetium or rhenium · CPC title

• C07D303/04 Primary

  containing only hydrogen and carbon atoms in addition to the ring oxygen atoms · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title