CPC VI -- Chemical Process Control VI

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© 2002 American Institute of Chemical Engineers (AIChE) and Computer Aids for Chemical Engineering Education (CACHE) Neither AIChE nor CACHE shall be responsible for statements or opinions advanced in their papers or printed in their publications. > Library of Congress Control Number: 2002102094 > > ISBN 0-8169-0869-9 All rights reserved whether the whole or part of the material is concerned, specifically those of translation, reprinting, re-use of illustrations, broadcasting, electronic networks, reproduction by photocopying machine or similar means, and storage of data in banks. Authorization to photocopy items for internal use, or the internal or personal use of specific clients, is granted by AIChE for libraries and other users registered with the Copyright Clearance Center Inc., 222 Rosewood Drive, Danvers, MA 01923. This consent does not extend to copying for general distribution, for advertising, for promotional purposes, for inclusion in a publication, or for resale. Articles published before 1978 are subject to the same copyright conditions. AIChE Symposium Series fee code: 0065-8812/1998. $15.00 per article.
Preface The sixth International Chemical Process Control meeting (CPC VI) was held January 7–12, 2001 at the Westward Look Resort in Tucson, Arizona. The uniqueness of the CPC meeting series in the process control community is illustrated by the following features: the meetings are held at five year intervals, all talks are invited and are organized in a single track so the entire audience can attend each presentation, and most importantly, a significant fraction of the audience, usually more than half, is comprised of leaders from the chemical process industries. The overall goal of the CPC conference series is to evaluate the current progress in this field and identify the new intellectual challenges and frontiers that may have fundamental impact on future industrial practice. At CPC VI, of the 135 registered attendees, about 65 were from the chemical process industries, and the rest were from universities and federal agencies. The program consisted of the following technical sessions with session organizers in parenthesis. • Opening Session (J. Brian Froisy) • Modeling and Identification (Jay H. Lee) • Life Sciences (Francis J. Doyle) • Control Theory (Frank Allgower) • Hybrid Systems (Manfred Morari) • Controller Performance Monitoring and Maintenance (Derrick J. Kozub) • Chemical Reactors/Separators (Lorenz T. Biegler and B. Wayne Bequette) • Modeling and Control of Complex Products (Babatunde A. Ogunnaike) • Contributed Paper Poster Session (Kenneth R. Muske) • Closing Session (James B. Rawlings) The meeting also included a Vendor and Software Display organized by S. Joe Qin. A detailed meeting summary has been compiled including graphical representation of detailed pre-session and post-session evaluations. This summary is is available at the meeting website: http://www.che.wisc.edu/cpc-6 Finally, we should attempt to draw conclusions from the meeting. These are the editors’ opinions, but are informed by the week long CPC VI meeting discussions. The chemical process control community (indeed the entire chemical engineering profession) is going through a transition period, in which the industries served by the iii chemical engineering profession are diversifying. During this period, it is essential that process control researchers continue to identify new opportunities in which applications of systems theory concepts provide significant added value. These proceedings document that the younger researchers in the community are already engaged in vigorous efforts to build significant collaborations to support these new application areas. Those activities portend well for the future health of this research community. Several people noted that discussions at previous CPCs were marked by more conflict than those at CPC VI, and one explanation seems to be that we have been extremely successful in bringing the best advanced control concepts and methods into practice during this short time period. We should not become victims of this success, but must embrace both the controversial new ideas, as well as the critical evaluation of these ideas, as we create the concepts that will sparkle at future CPC meetings. Secondly, it seems timely to return to and embrace the broad meaning of systems theory and the tools it brings to chemical process modeling, dynamics and control. The significant distinction in systems engineering is whether we address the online challenge—using data and models for best real time operations decisions, or whether we address the offline challenge—to synthesize and design the new products and the new processes. Other less vital distinctions and categories that have grown up over the years do not serve us well in the current climate, because they dilute rather than deepen our focus. Finally, as representatives of the chemical engineering profession with some of the closest connections to applications and technology, this community has a unique opportunity to play a leadership role in identifying the significant new directions in areas such as: computing tools, information processing, and measurement technologies, to name just three areas in which we are all experts. Given the rapid pace of technological change, the chemical engineering profession needs people who can distinguish the fundamental changes that present new opportunities from the blinding array of incremental and ephemeral changes. This community should embrace the challenge of providing that leadership. We have the knowledge, the tools, the experience, the vision and the people to play a key role. James B. Rawlings, University of Wisconsin Babatunde A. Ogunnaike, DuPont John W. Eaton, University of Wisconsin
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Page 5 and 6: Contents INVITED PAPERS Opening Ses
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44 Ton C. Backx development related
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46 Ton C. Backx input manipulations
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48 Ton C. Backx Operating Constrain
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50 Ton C. Backx tion (Verhaegen and
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52 Ton C. Backx DENS DENS DENS DENS
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54 Ton C. Backx Proceedings of Chem
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56 Sten Bay Jørgensen and Jay H. L
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76 James S. Schwaber, Francis J. Do
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Computer-Aided Design of Metabolic
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84 Klaus Mauch, Stefan Buziol, Joac
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Neuro-Dynamic Programming: An Overv
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94 Dimitri P. Bertsekas capture the
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96 Dimitri P. Bertsekas and other p
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98 Jan C. Willems models. Whence we
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100 Jan C. Willems Of particular in
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102 Jan C. Willems ever, there are
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104 Jan C. Willems these questions
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106 Jan C. Willems hinges damper do
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108 Jan C. Willems tems greatly enh
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110 Eduardo D. Sontag and u ∞ = (
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112 Eduardo D. Sontag ω3, I2u1 = (
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114 Eduardo D. Sontag Integral-Inpu
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116 Eduardo D. Sontag where the γi
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118 Eduardo D. Sontag was instrumen
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120 Eduardo D. Sontag stability,”
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122 Stefan Kowalewski refers to mod
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124 Stefan Kowalewski is empty fill
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126 Stefan Kowalewski y y 100 90 80
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128 Stefan Kowalewski of its own wh
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130 Stefan Kowalewski niques from o
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132 Stefan Kowalewski correctness o
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134 Stefan Kowalewski algorithmic a
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Hybrid System Analysis and Control
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138 Manfred Morari Relation Logic (
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140 Manfred Morari optima, but only
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142 Manfred Morari Figure 4: Reacha
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144 Manfred Morari Logic state Heat
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146 Manfred Morari x 2 #3 #4 5 4 3
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148 Manfred Morari Appendix HYSDEL
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Discrete Optimization Methods and t
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152 Ignacio E. Grossmann, Susara A.
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170 Lane Desborough and Randy Mille
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Multivariate Controller Performance
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192 Sirish L. Shah, Rohit Patwardha
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Recent Developments in Controller P
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210 Thomas J. Harris and Christophe
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224 Efstratios N. Pistikopoulos and
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240 Karsten-U. Klatt, Guido Dünneb
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256 D. Bonvin, B. Srinivasan and D.
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Dynamics and Control of Cell Popula
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276 Prodromos Daoutidis and Michael
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Control of Product Quality in Polym
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292 Francis J. Doyle III, Masoud So
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308 Richard D. Braatz and Shinji Ha
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Linking Control Strategy Design and
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330 James J. Downs effective tool.
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332 James J. Downs FC FY < DP Figur
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334 James J. Downs Heat Input Feed
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336 James J. Downs FC DP Figure 6:
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338 James J. Downs Furnace Furnace
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340 James J. Downs Water Refining s
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Evolution of an Industrial Nonlinea
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344 Robert E. Young, R. Donald Bart
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Emerging Technologies for Enterpris
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354 Rudolf Kulhav´y, Joseph Lu and
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A Definition for Plantwide Controll
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366 Surya Kiran Chodavarapu and Ale
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368 Surya Kiran Chodavarapu and Ale
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370 Nael H. El-Farra and Panagiotis
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372 Nael H. El-Farra and Panagiotis
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Rolf Findeisen ∗ and Frank Allgö
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376 Rolf Findeisen, Frank Allgöwer
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378 Rolf Findeisen, Frank Allgöwer
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380 Guruprasad A. Giridharan and Mi
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382 Guruprasad A. Giridharan and Mi
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Assessment of Performance for Singl
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386 Hsiao-Ping Huang and Jyh-Cheng
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388 Hsiao-Ping Huang and Jyh-Cheng
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390 Joshua M. Kanter, Warren D. Sei
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392 Joshua M. Kanter, Warren D. Sei
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394 Truls Larsson, Sigurd Skogestad
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396 Truls Larsson, Sigurd Skogestad
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Robust Passivity Analysis and Desig
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400 Huaizhong Li, Peter L. Lee and
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402 Huaizhong Li, Peter L. Lee and
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404 Tore Lid, Stig Strand and Sigur
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406 Tore Lid, Stig Strand and Sigur
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Analysis of a Class of Statistical
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410 Kenneth R. Muske and Conner S.
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412 Kenneth R. Muske and Conner S.
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414 Michael Nikolaou and Mohan R. C
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416 Michael Nikolaou and Mohan R. C
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Abstract Efficient Nonlinear Model
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420 Robert S. Parker The weighting
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422 Robert S. Parker distillation),
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424 Stéphane Renou, Michel Perrier
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426 Stéphane Renou, Michel Perrier
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Steady State Multiplicity and Stabi
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430 Iván E. Rodríguez, Alex Zheng
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432 Iván E. Rodríguez, Alex Zheng
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434 Matthew J. Tenny, James B. Rawl
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436 Matthew J. Tenny, James B. Rawl
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Industrial Experience with State-Sp
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440 Ernest F. Vogel and James J. Do
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442 Ernest F. Vogel and James J. Do
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444 Zhaoyang Wan and Mayuresh V. Ko
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446 Zhaoyang Wan and Mayuresh V. Ko
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Time Series Reconstruction from Qua
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450 M. Wang, S. Saleem and N. F. Th
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452 M. Wang, S. Saleem and N. F. Th
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454 Author Index Schmid, Joachim, 8
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456 Subject Index Mixed-integer dyn
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CPC VI -- Chemical Process Control VI

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