The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Feb. 16, 2016

Filed:

Mar. 02, 2010
Applicants:

Timothy Morrison, Houston, TX (US);

Michael Sugars, Elgin, TX (US);

Inventors:

Timothy Morrison, Houston, TX (US);

Michael Sugars, Elgin, TX (US);

Assignee:

ROCKWELL AUTOMATION TECHNOLOGIES, INC., Mayfield Heights, OH (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
G01N 35/08 (2006.01); G05B 13/04 (2006.01); F25J 3/02 (2006.01); G05B 19/418 (2006.01);
U.S. Cl.
CPC ...
G05B 13/048 (2013.01); F25J 3/0219 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 3/0242 (2013.01); F25J 3/0247 (2013.01); F25J 3/0295 (2013.01); G05B 19/41865 (2013.01); F25J 2210/12 (2013.01); F25J 2215/62 (2013.01); F25J 2215/64 (2013.01); F25J 2215/66 (2013.01); F25J 2270/02 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01); F25J 2270/88 (2013.01); F25J 2280/50 (2013.01); Y10T 436/12 (2015.01);
Abstract

System and method for chemical manufacture utilizing a dynamic optimizer for a chemical process including upstream and downstream processes. The dynamic optimizer includes a maximum feed calculator, operable to receive one or more local constraints on the downstream processes and one or more model offsets, and execute steady state models for the downstream processes in accordance with the local constraints and the offsets to determine maximum feed capacities of the downstream processes; and a feed coordinator, operable to receive the maximum feed capacities, and execute steady state models for the upstream processes in accordance with the maximum feed capacities and a specified objective function, subject to global constraints, to determine upstream production parameters for the upstream processes, which are usable to control the upstream processes to provide feeds to the downstream processes in accordance with the determined maximum feeds and the objective function subject to the global constraints.


Find Patent Forward Citations

Loading…