Practical Approaches to Nonlinear Control
暂无分享,去创建一个
[1] C. Kravaris,et al. Geometric methods for nonlinear process control. 1. Background , 1990 .
[2] R. Pearson. Nonlinear Input/Output Modeling , 1994 .
[3] Tore Hägglund,et al. Automatic Tuning and Adaptation for PID Controllers—A Survey , 1992 .
[4] K Y San,et al. The design of controllers for batch bioreactors , 1988, Biotechnology and bioengineering.
[5] Hannu T. Toivonen,et al. Multimodel robust control of nonlinear plants: a case study , 1999 .
[6] S. J. Qin,et al. A multi-region fuzzy logic controller for controlling processes with nonlinear gains , 1993, Proceedings of 8th IEEE International Symposium on Intelligent Control.
[7] Evanghelos Zafiriou,et al. Robust process control , 1987 .
[8] Martin Gullaian,et al. Titration Curve Estimation for Adaptive pH Control , 1990, 1990 American Control Conference.
[9] Dale E. Seborg,et al. Low-Order, Nonlinear, Dynamic Models for Distillation Columns , 1986, 1986 American Control Conference.
[10] P. Gahinet,et al. A convex characterization of gain-scheduled H∞ controllers , 1995, IEEE Trans. Autom. Control..
[11] S. Engell,et al. Nonlinear Control of a Non-Minimum-Phase CSTR , 1993, 1993 American Control Conference.
[12] Cheng-Ching Yu,et al. Autotuning of gain-scheduled pH control : an experimental study , 1995 .
[13] Thomas E. Marlin,et al. Process Control: Designing Processes and Control Systems for Dynamic Performance , 1995 .
[14] Luigi Marini,et al. Low‐density polyethylene vessel reactors: Part II: A novel controller , 1984 .
[15] Michael K. F. Knoop,et al. Nonlinear PI-controller design for a continuous-flow furnace via continuous gain scheduling , 1994 .
[16] Thomas J. McAvoy,et al. Gain scheduling for composition control of distillation columns , 1985 .
[17] Dale E. Seborg,et al. Nonlinear Process Control , 1996 .
[18] Wilson J. Rugh,et al. Output regulation with derivative information , 1995, IEEE Trans. Autom. Control..
[19] William L. Luyben,et al. Experimental Evaluation of Nonlinear Cascade Controllers for Batch Reactors , 1972 .
[20] Manfred Morari,et al. Model predictive control: Theory and practice - A survey , 1989, Autom..
[21] Dale E. Seborg,et al. Feedback linearizing control , 1997 .
[22] Gilles Trystram,et al. Dynamics analysis and control strategy for a mixed flow corn dryer , 1997 .
[23] A. Packard. Gain scheduling via linear fractional transformations , 1994 .
[24] Thomas E Marlin,et al. Process Control , 1995 .
[25] B. G. Liptak. Controlling and optimizing chemical reactors , 1986 .
[26] Isaac Kaminer,et al. A velocity algorithm for the implementation of gain-scheduled controllers , 1995, Autom..
[27] Wilson J. Rugh,et al. Gain scheduling dynamic linear controllers for a nonlinear plant , 1995, Autom..
[28] M. J. Whatley,et al. Adaptive gain improves reactor control , 1984 .
[29] Ka-Yiu San,et al. Application of Gain Scheduling to the Control of Batch Bioreactors , 1987, 1987 American Control Conference.
[30] Wonhui Cho,et al. Control system design based on a nonlinear first-order plus time delay model , 1997 .
[31] B. Bequette. Nonlinear control of chemical processes: a review , 1991 .
[32] Dale E. Seborg,et al. Control Strategies for Nonlinear Multivariable Systems with Time Delays , 1986, 1986 American Control Conference.
[33] M. Morari,et al. Understanding the Dynamic Behavior of Distillation Columns , 1988 .
[34] M. Morari,et al. LV-Control of a high-purity distillation column , 1987 .
[35] S. Engell,et al. Nonlinear Control of Neutralization Processes by Gain-Scheduling Trajectory Control , 1996 .
[36] Francis J. Doyle,et al. Dynamic gain scheduled process control , 1998 .
[37] Costas Kravaris,et al. Model-based synthesis of nonlinear PI and PID controllers , 1996 .
[38] William L. Luyben,et al. Nonlinear and Nonconventional Liquid Level Controllers , 1980 .
[39] T. Edgar,et al. A New Fuzzy Gain Scheduling Algorithm for Process Control , 1992, 1992 American Control Conference.
[40] William L. Luyben,et al. Nonlinear dynamic matrix control for high‐purity distillation columns , 1988 .
[41] Willy Wojsznis,et al. Flexible gain scheduler , 1994 .
[42] D. Seborg,et al. Control strategy for single-input single-output non-linear systems with time delays , 1988 .
[43] Michael Athans,et al. Guaranteed properties of gain scheduled control for linear parameter-varying plants , 1991, Autom..
[44] Masayoshi Tomizuka,et al. Fuzzy gain scheduling of PID controllers , 1993, IEEE Trans. Syst. Man Cybern..
[45] J. F. Steadman. Control techniques for nonlinear chemical processes , 1978 .
[46] Wilson J. Rugh,et al. Analytical Framework for Gain Scheduling , 1990, 1990 American Control Conference.
[47] Tore Hägglund,et al. Automatic tuning of simple regulators with specifications on phase and amplitude margins , 1984, Autom..
[48] Thomas J. McAvoy,et al. Application of Dynamic Matrix Control to Moderate and High Purity Distillation Towers. , 1987 .
[49] Pierre Apkarian,et al. Parameter Varying Control of a High-Performance Aircraft , 1996 .
[50] André L. Tits,et al. Optimal averaging level control , 1986 .
[51] Ahmet Palazoglu,et al. Impact of model uncertainty descriptions for high-purity distillation control , 1988 .
[52] Cheng Ling,et al. Experimental verification of model-based fuzzy gain scheduling technique , 1994, Proceedings of 1994 American Control Conference - ACC '94.
[53] Cheng-Ching Yu,et al. Automatic tuning and gain scheduling for pH control , 1993 .
[54] Manfred Morari,et al. Linear parameter varying model predictive contr for steam generator level control , 1997 .
[55] Arthur Jutan. A nonlinear pi(d) controller , 1989 .
[56] W. Rugh. Design of nonlinear PID controllers , 1987 .
[57] Christos Georgakis,et al. On the use of extensive variables in process dynamics and control , 1986 .