IP Library Granted Patent US 8,290,626
Granted Patent B2
US 8,290,626 · App. 11/852,713 · Granted Oct 16, 2012

Chemical process optimization method that considers chemical process plant safety

Assignee: SD Lizenzverwertungsgesellschadt mbH & Co KG
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Quick Facts
Patent No.
US 8,290,626
App. No.
11/852,713
Granted
Oct 16, 2012
Kind
B2
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 (29)

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, wherein said plurality of sets of proposed process conditions includes employing a same initial reaction pressure and temperature for each set, while varying concentration of at least one reactant gas used for the particular chemical process in each set;

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 within the particular chemical process, to provide a plurality of pressure rise rates that corresponds with the plurality of sets of proposed process conditions, wherein said plurality of sets of proposed process conditions includes employing a same initial reaction pressure and temperature for each set, while varying concentration of at least one reactant gas used for the particular chemical process in each set;

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, wherein said plurality of proposed process conditions includes employing a same initial reaction pressure and temperature for each set, while varying concentration of at least one reactant gas used for the particular chemical process in each set;

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 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.

18. The method of claim 17 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.

19. The method of claim 18 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.

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME AND ADDRESS PREVIOUSLY RECORDED ON REEL 019803 FRAME 0735. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE PREVIOUSLY RECORDED. ASSIGNOR(S) HEREBY CONFIRM ASSIGNEE: SD LIZENZVERWERTUNGSGESELLSCHAFT MBH AND CO.. Recorded Jun 13, 2008
From: BILLIG, BARRY J.; SULLIVAN, JOHN JAMES
To: SD LIZENZVERWERTUNGSGESELLSCHAFT MBH & CO. KG
Reel/Frame 021094/0419 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 10, 2007
From: BILLING, BARRY JAY; SULLIVAN, JOHN JAMES
To: INTERNATIONAL BUSINESS MACHINES CORPORATION
Reel/Frame 019803/0735 →
Continuity (1)
Related Publication 20090069944A1 · Mar 12, 2009