Chapter A7 Analysing the controllability of nonlinear process systems

[1]  Frank Allgöwer,et al.  A quasi-infinite horizon nonlinear model predictive control scheme with guaranteed stability , 1997, 1997 European Control Conference (ECC).

[2]  S. Skogestad.  DYNAMICS AND CONTROL OF DISTILLATION COLUMNS A tutorial introduction , 1997 .

[3]  Ian David Lockhart Bogle,et al.  Robust operation of fed batch fermenters , 1998 .

[4]  David D. Brengel,et al.  Nonlinear analysis in process design. Why overdesign to avoid complex nonlinearities , 1990 .

[5]  J. A. Bandoni,et al.  Effect of disturbances in optimizing control: Steady‐state open‐loop backoff problem , 1996 .

[6]  Sigurd Skogestad,et al.  Selecting the best distillation control configuration , 1990 .

[7]  Sigurd Skogestad,et al.  Design of resilient processing plants-IX. Effect of model uncertainty on dynamic resilience , 1987 .

[8]  Efstratios N. Pistikopoulos,et al.  Simultaneous design and control optimisation under uncertainty , 2000 .

[9]  J. A. Bandoni,et al.  Integrated flexibility and controllability analysis in design of chemical processes , 1997 .

[10]  Christodoulos A. Floudas,et al.  Analyzing the interaction of design and control—1. A multiobjective framework and application to binary distillation synthesis , 1994 .

[11]  J. D. Perkins,et al.  An algorithmic method for the selection of multivariable process control structures , 2002 .

[12]  B. Bequette,et al.  Model predictive control of processes with input multiplicities , 1995 .

[13]  Ignacio E. Grossmann,et al.  An index for operational flexibility in chemical process design. Part I: Formulation and theory , 1985 .

[14]  T. McAvoy.  Synthesis of Plantwide Control Systems Using Optimization , 1999 .

[15]  Ian Postlethwaite,et al.  Multivariable Feedback Control: Analysis and Design , 1996 .

[16]  John D. Perkins,et al.  Optimization as a tool for design/control integration , 1994 .

[17]  Thomas F. Fairgrieve,et al.  AUTO 2000 : CONTINUATION AND BIFURCATION SOFTWARE FOR ORDINARY DIFFERENTIAL EQUATIONS (with HomCont) , 1997 .

[18]  E. Bristol.  On a new measure of interaction for multivariable process control , 1966 .

[19]  L. B. Koppel.  Input multiplicities in nonlinear, multivariable control systems , 1982 .

[20]  Efstratios N. Pistikopoulos,et al.  The interactions of design and control: double-effect distillation , 2000 .

[21]  Daniel R. Lewin,et al.  Dynamic controllability and resiliency diagnosis using steady state process flowsheet data , 1996 .

[22]  I. David L. Bogle,et al.  Controllability evaluation for nonminimum phase‐processes with multiplicity , 2001 .

[23]  Cheng-Ching Yu,et al.  Relative disturbance gain array , 1992 .

[24]  Geoffrey W. Barton,et al.  A condition number scaling policy for stability robustness analysis , 1988 .

[25]  David Bogle,et al.  Study on nonminimum phase behaviour and optimal operation , 1997 .

[26]  Efstratios N. Pistikopoulos,et al.  Optimal design of dynamic systems under uncertainty , 1996 .

[27]  V. D. Dimitriadis,et al.  Flexibility Analysis of Dynamic Systems , 1995 .

[28]  S. D. Chenery,et al.  Process controllability analysis using linear programming , 1998 .