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E-Book

E-Book, Englisch, Band 45, 473 Seiten

Reihe: Automation and Control Engineering

Zhang Quantitative Process Control Theory


1. Auflage 2011
ISBN: 978-1-4398-5561-4
Verlag: CRC Press
Format: PDF
Kopierschutz: Adobe DRM (»Systemvoraussetzungen)

E-Book, Englisch, Band 45, 473 Seiten

Reihe: Automation and Control Engineering

ISBN: 978-1-4398-5561-4
Verlag: CRC Press
Format: PDF
Kopierschutz: Adobe DRM (»Systemvoraussetzungen)



Quantitative Process Control Theory explains how to solve industrial system problems using a novel control system design theory. This easy-to-use theory does not require designers to choose a weighting function and enables the controllers to be designed or tuned for quantitative engineering performance indices such as overshoot.

In each chapter, a summary highlights the main problems and results and exercises improve and test your understanding of the material. Mathematical proofs are provided for almost all the results while examples are based on actual situations in industrial plants involving a paper-making machine, heat exchanger, hot strip mill, maglev, nuclear reactor, distillation column/heavy oil fractionator, jacket-cooled reactor, missile, helicopter/plane, and anesthesia.

Developed from the author’s many years of research, this book takes a unique, practical approach for efficiently solving single-input and single-output (SISO) and multiple-input and multiple-output (MIMO) control system design issues for quantitative performance indices. With much of the material classroom-tested, the text is suitable for advanced undergraduate and graduate students in engineering, beginning researchers in robust control, and more seasoned engineers wanting to learn new design techniques.

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Zielgruppe


Graduate students and researchers in process control and chemical engineering.


Autoren/Hrsg.


Weitere Infos & Material


Introduction

A Brief History of Control Theory

Design of Feedback Control Systems

Consideration on Control System Design

What This Book Is About

Classical Analysis Methods

Process Dynamic Responses

Rational Approximations of Time Delay

Time Domain Performance Indices

Frequency Response Analysis

Transformation of Two Commonly Used Models

Design Requirements and Controller Comparison

Essentials of the Robust Control Theory

Norms and System Gains

Internal Stability and Performance

Controller Parameterization

Robust Stability and Robust Performance

Robustness of the System with Time Delay

H8 PID Controllers for Stable Plants

Traditional Design Methods

H8 PID Controller for the First-Order Plant

The H8 PID Controller and the Smith Predictor

Quantitative Performance and Robustness

H8 PID Controller for the Second-Order Plant
All Stabilizing PID Controllers for Stable Plants

H2 PID Controllers for Stable Plants

H2 PID Controller for the First-Order Plant

Quantitative Tuning of H2 PID Controller

H2 PID Controller for the Second-Order Plant

Control of Inverse Response Processes

PID Controller Based on the Maclaurin Series Expansion

PID Controller with the Best Achievable Performance

Choice of the Filter

Control of Stable Plants

The Quasi-H8 Smith Predictor

The H2 Optimal Controller and the Smith Predictor

Equivalents of the Optimal Controller

PID Controller and High-Order Controllers

Choice of the Weighting Function

Simplified Tuning for Quantitative Robustness

Control of Integrating Plants

Feature of Integrating Systems

H8 PID Controller for Integrating Plants

H2 PID Controller for Integrating Plants

Controller Design for General Integrating Plants

Maclaurin PID Controller for Integrating Plants

The Best Achievable Performance of a PID Controller

Control of Unstable Plants

Controller Parameterization for General Plants

H8 PID Controller for Unstable Plants

H2 PID Controller for Unstable Plants

Performance Limitation and Robustness

Maclaurin PID Controller for Unstable Plants

PID Design for the Best Achievable Performance
All Stabilizing PID Controllers for Unstable Plants

Complex Control Strategies

The 2DOF Structure for Stable Plants

The 2DOF Structure for Unstable Plants

Cascade Control

An Anti-Windup Structure

Feedforward Control

Optimal Input Disturbance Rejection

Control of Plants with Multiple Time Delays

Analysis of MIMO Systems

Zeros and Poles of a MIMO Plant

Singular Values

Norms for Signals and Systems

Nominal Stability and Performance

Robust Stability of MIMO Systems

Robust Performance of MIMO Systems

Classical Design Methods for MIMO Systems

Interaction Analysis

Decentralized Controller Design

Decoupler Design

Quasi-H8 Decoupling Control

Diagonal Factorization for Quasi- H8 Control

Quasi- H8 Controller Design

Analysis for Quasi- H8 Control Systems

Increasing Time Delays for Performance Improvement

A Design Example for Quasi- H8 Control

Multivariable PID Controller Design

H2 Decoupling Control

Controller Parameterization for MIMO Systems

Diagonal Factorization for H2 Control

H2 Optimal Decoupling Control

Analysis for H2 Decoupling Control Systems

Design Examples for H2 Decoupling Control

Multivariable H2 Optimal Control

Factorization for Simple RHP Zeros

Construction Procedure of Factorization

Factorization for Multiple RHP Zeros
Analysis and Computation

Solution to the H2 Optimal Control Problem

Filter Design

Examples for H2 Optimal Controller Designs

Bibliography
Index

A Summary, Exercises, Notes, and References appear at the end of each chapter.


Weidong Zhang is a professor at Shanghai Jiaotong University. Dr. Zhang has authored more than 200 refereed papers and holds 15 patents. His research interests include control theory and its applications, embedded systems, and wireless sensor networks.



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