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US007877l54B2

(12) Ullitfild States Patent (10) Patent No.: US 7,877,154 B2 Blevins et al. (45) Date of Patent: Jan. 25, 2011 (54) METHOD AND SYSTEM FOR 2006/0058899 A1 * 3/2006 Boyden et al. .............. .. 700/44

CONTROLLING A BATCH PROCESS

(75) Inventors: Terrence L. Blevins, Round Rock, TX
(US); Gregory K. McMillan, Austin,
TX (U S); Michael A. Boudreau, Austin,
TX (US)
(73) Assignee: Fisher-Rosemount Systems, Inc.,
Austin, TX (U S)
( * ) Notice: Subject to any disclaimer, the term of this
patent is extended or adjusted under 35
U.S.C. l54(b) by 553 days.
(21) Appl.No.: 11/241,157
(22) Filed: Sep. 30, 2005
(65) Prior Publication Data
US 2007/0078530 A1 Apr. 5, 2007
(51) Int. Cl.
G05B 13/02 (2006.01)
(52) U.S. Cl. ........................... .. 700/31; 700/29; 700/52;
700/53
(58) Field of Classification Search ........... .. 700/29-32,
700/52, 53, 44, 45, 46; 703/2
See application file for complete search history.
(56) References Cited
U.S. PATENT DOCUMENTS
6,445,963 Bl 9/2002 Blevins et al.
6,721,609 B1 4/2004 Wojsznis et al.
6,760,716 B1* 7/2004 Ganesarnoorthiet al. 706/21
6,901,308 Bl 5/2005 Hamada et al.
2002/0107604 Al 8/2002 Riley et al.
2004/0049299 Al 3/2004 Wojsznis et al.
2004/0243380 Al * 12/2004 Blevins et al. .............. .. 703/22
2004/0249483 Al * 12/2004 Wojsznis et al. ............ .. 700/31
2005/0154477 Al 7/2005 Martin et al.

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FOREIGN PATENT DOCUMENTS

CN 1416540 A 5/2003
WO WO-01/46762 6/2001
WO WO-01/67189 9/2001
WO WO01/67189 A1 9/2001

OTHER PUBLICATIONS

U.S. Appl. No. 09/510,053, filed Feb. 22, 2000, Nixon et al.

Search Report for Application No. GB0618442.8, dated Jan. 18, 2007.

L. Rueda, “Modeling and Control of Multicomponent Distillation
Systems Separating Highly Non-Ideal Mixtures”, Dissertation, Uni-
versity of Texas at Austin (2005).

L. Rueda et al ., “On-line Parameter Estimation and Control for a Pilot
Scale Distillation Column,” Presented at AlChE Annual Meeting,
Austin, TX (Nov. 2004).

(Continued)

Primary Examiner—Albert DeCady

Assistant Examiner—Steven R Garland

(74) Attorney, Agent, or Firm—Marshall, Gerstein & Borun LLP

(57) ABSTRACT

A first principles model may be used to simulate a batch process, and the first principles model may be used to configure a multiple-input/multiple-output control routine for controlling the batch process. The first principles model may generate estimates of batch parameters that camiot, or are not, measured during operation of the actual batch process. An example of such a parameter may be a rate of change of a component (e.g., a production rate, a cell growth rate, etc.) of the batch process. The first principles model and the configured multiple-input/multiple-output control routine may be used to facilitate control of the batch process.

25 Claims, 10 Drawing Sheets

42

[merged small][graphic]

QTHER PUBLICATIQNS Examination Report for Great Britain Application No. 0618442.8,

First Office Action for corresponding Chinese Application No. dated Aug272009'

2()()61()131751,2, dared Jan, 3, 2()1(), Combined Search and Examination Report for Great Britain AppliCombined Search and Examination Report under Sections 17 and 0611011 N0- 1003332-7, 1161611 M6f- Z2, Z010

18(3) issued in GB 1 00 8266.7 application by United Kingdom Patent

Office dated Jun. 7, 2010. * cited by examiner

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