CHEMICAL PROCESS OPTIMIZATION METHOD THAT CONSIDERS CHEMICAL PROCESS PLANT SAFETY

• US 20090069944A1
• Filed: 09/10/2007
• Published: 03/12/2009
• Est. Priority Date: 09/10/2007
• Status: Active Grant

• Current Assignee: International Business Machines Corporation, SD Lizenzverwertungsgesellschaft mbH & Co. KG
• Original Assignee: SD Lizenzverwertungsgesellschaft mbH & Co. KG
• Inventors: Sullivan, John James, Billig, Barry Jay
• Granted Patent: US 8,290,626 B2
• Time in Patent Office: Days
• US Class Current: 700/268
• CPC Class Codes: B01J 2208/00274 involving reactant vapours
• CPC Class Codes: B01J 2208/00539 Pressure
• CPC Class Codes: B01J 2219/00259 Preventing runaway of the chemical reaction
• CPC Class Codes: B01J 2219/00263 Preventing explosion of the chemical mixture
• CPC Class Codes: B01J 2219/0027 Pressure relief
• CPC Class Codes: B01J 8/025 in a cylindrical shaped bed
• CPC Class Codes: G05B 9/02 electric

Abstract

A method for assuring safety of a particular chemical process plant includes measuring, for each of a plurality of sets of proposed process conditions for a particular chemical process within the particular chemical process plant, a pressure rise rate following a deliberate contained ignition of at least one material used within the particular chemical process. From the resulting plurality of pressure rise rates that corresponds with the plurality of sets of proposed process conditions a particular pressure rise rate that allows for a safe operation of the particular chemical reaction within the particular chemical process plant may be selected. The particular chemical process may be implemented within the particular chemical process plant while using a particular set of process conditions from the plurality of sets of process conditions that corresponds with the selected pressure rise rate. As an adjunct, the particular chemical reaction may also be subsequently and additionally optimized with respect to an ancillary parameter, such as product yield or feedstock utilization.

Claims

1. A method for safely operating a chemical process plant comprising:

measuring, for each of a plurality of sets of proposed process conditions for a particular chemical process within a particular chemical process plant, a pressure rise rate following a deliberate contained ignition of at least one material within the particular chemical process, to provide a plurality of pressure rise rates that corresponds with the plurality of sets of proposed process conditions;

selecting from the plurality of pressure rise rates a particular pressure rise rate that allows for a safe operation of the particular chemical process within the particular chemical process plant; and

implementing the particular chemical process within the particular chemical process plant while using a particular set of process conditions from the plurality of sets of reactor conditions that corresponds with the particular pressure rise rate from the plurality of pressure rise rates.

2. The method of claim 1 wherein the chemical process plant comprises a batch chemical process plant.

3. The method of claim 1 wherein the chemical process plant comprises a continuous chemical process plant.

4. The method of claim 1 wherein the particular chemical process comprises an organic chemical process.

5. The method of claim 4 wherein the organic chemical process comprises an oxidation process.

6. The method of claim 1 wherein the particular chemical process comprises an inorganic chemical process.

7. The method of claim 1 wherein the deliberate contained ignition and the measuring of the pressure rise rate is undertaken using a test apparatus separate from the particular chemical process plant.

8. A method for safely operating a chemical process plant comprising:

measuring, for each of a plurality of sets of proposed process conditions for a particular chemical process within a particular chemical process plant, a pressure rise rate following a deliberate contained ignition of at least one material with the particular chemical process, to provide a plurality of pressure rise rates that corresponds with the plurality of sets of proposed process conditions;

selecting from the plurality of pressure rise rates a sub-plurality of pressure rise rates that allows for a safe operation of the particular chemical process within the particular chemical process plant;

determining for each pressure rise rate within the sub-plurality of pressure rise rates a value of an ancillary parameter for the particular chemical process, to thus provide a sub-plurality of values of the ancillary parameter for the particular chemical process that correspond with the sub-plurality of pressure rise rates; and

implementing the particular chemical process within the particular chemical process plant while using a particular set of process conditions from the plurality of sets of proposed process conditions that corresponds with a particular pressure rise rate from the sub-plurality of pressure rise rates that is optimized with respect to a particular value of the ancillary parameter selected from the sub-plurality of values of the ancillary parameter.

9. The method of claim 8 wherein the chemical process plant comprises a batch chemical process plant.

10. The method of claim 8 wherein the chemical process plant comprises a continuous chemical process plant.

11. The method of claim 8 wherein the particular chemical process comprises an organic chemical process.

12. The method of claim 11 wherein the organic chemical process comprises an oxidation process.

13. The method of claim 8 wherein the particular chemical process comprises an inorganic chemical process.

14. The method of claim 8 wherein the deliberate contained ignition and the measuring of the pressure rise rate is undertaken using a test apparatus separate from the particular chemical process plant.

15. A method for safely operating an olefin oxidation chemical process plant comprising:

measuring, for each of a plurality of sets of proposed process conditions for an olefin oxidation chemical process within a particular chemical process plant, a pressure rise rate following a deliberate contained ignition of at least one material within the olefin oxidation chemical process, to provide a plurality of pressure rise rates that corresponds with the plurality of sets of proposed process conditions;

selecting from the plurality of pressure rise rates a particular pressure rise rate that allows for a safe operation of the olefin oxidation chemical process within the particular chemical process plant; and

implementing the olefin oxidation chemical process within the particular chemical process plant while using a particular set of process conditions from the plurality of sets of process conditions that corresponds with the particular pressure rise rate from the plurality of pressure rise rates.

16. The method of claim 15 wherein the olefin oxidation reaction comprises an ethylene epoxidation reaction.

17. The method of claim 15 wherein the olefin oxidation reaction comprises other than an ethylene epoxidation reaction.

18. The method of claim 15 wherein the selecting provides a sub-plurality of pressure rise rates that allow for safe operation of the olefin oxidation chemical process within the particular chemical process plant.

19. The method of claim 18 further comprising determining for each pressure rise rate within the sub-plurality of pressure rise rates a value of an ancillary parameter for the olefin oxidation chemical process, to thus provide a sub-plurality of values of the ancillary parameter for the olefin oxidation chemical process that correspond with the sub-plurality of pressure rise rates.

20. The method of claim 19 wherein the implementing the olefin oxidation chemical process within the particular chemical process plant uses a particular set of process conditions from the plurality of sets of proposed process conditions that corresponds with a particular pressure rise rate from the sub-plurality of pressure rise rates that is optimized with respect to a particular value of the ancillary parameter selected from the sub-plurality of values of the ancillary parameter.