Advanced Chemical Process Control 1st Edition by Morten Hovd ISBN 9783527352234 3527352236

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ISBN 10: 3527352236
ISBN 13: 9783527352234
Author: Morten Hovd

Advanced Chemical Process Control 1st Edition Table of contents:

I.1 Why Is Chemical Process Control Needed?

I.2 What Knowledge Does a chemical Process Control Engineer need?

I.3 What Makes Chemical Process Control Unique?

I.4 The Structure of Control Systems in the Chemical Process Industries

I.5 Notation

Notes

1 Mathematical and Control Theory Background

1.1 Introduction

1.2 Models for Dynamical Systems

1.3 Analyzing Linear Dynamical Systems

1.4 Poles and Zeros of Transfer Functions

1.5 Stability

Problems

References

Notes

2 Control Configuration and Controller Tuning

2.1 Common Control Loop Structures for the Regulatory Control Layer

2.2 Input and Output Selection

2.3 Control Configuration

2.4 Tuning of Decentralized Controllers

Problems

References

Notes

3 Control Structure Selection and Plantwide Control

3.1 General Approach and Problem Decomposition

3.2 Regulatory Control

3.3 Determining Degrees of Freedom

3.4 Selection of Controlled Variables

3.5 Selection of Manipulated Variables

3.6 Selection of Measurements

3.7 Mass Balance Control and Throughput Manipulation

Problems

References

Notes

4 Limitations on Achievable Performance

4.1 Performance Measures

4.2 Algebraic Limitations

4.3 Control Performance in Different Frequency Ranges

4.4 Bounds on Closed‐Loop Transfer Functions

4.5 ISE Optimal Control

4.6 Bandwidth and Crossover Frequency Limitations

4.7 Bounds on the Step Response

4.8 Bounds for Disturbance Rejection

4.9 Limitations from Plant Uncertainty

Problems

References

Notes

5 Model‐Based Predictive Control

5.1 Introduction

5.2 Formulation of a QP Problem for MPC

5.3 Step‐Response Models

5.4 Updating the Process Model

5.5 Disturbance Handling and Offset‐Free Control

5.6 Feasibility and Constraint Handling

5.7 Closed‐Loop Stability with MPC Controllers

5.8 Target Calculation

5.9 Speeding up MPC Calculations

5.10 Robustness of MPC Controllers

5.11 Using Rigorous Process Models in MPC

5.12 Misconceptions, Clarifications, and Challenges

Problems

References

Notes

6 Some Practical Issues in Controller Implementation

6.1 Discrete‐Time Implementation

6.2 Pure Integrators in Parallel

6.3 Anti‐Windup

6.4 Bumpless Transfer

Problems

References

7 Controller Performance Monitoring and Diagnosis

7.1 Introduction

7.2 Detection of Oscillating Control Loops

7.3 Oscillation Diagnosis

7.4 Plantwide Oscillations

7.5 Control Loop Performance Monitoring

7.6 Multivariable Control Performance Monitoring

7.7 Some Issues in the Implementation of Control Performance Monitoring

7.8 Discussion

Problems

References

Notes

8 Economic Control Benefit Assessment

8.1 Optimal Operation and Operational Constraints

8.2 Economic Performance Functions

8.3 Expected Economic Benefit

8.4 Estimating Achievable Variance Reduction

8.5 Worst‐Case Backoff Calculation

References

Note

A Fourier–Motzkin Elimination

B Removal of Redundant Constraints

Reference

C The Singular Value Decomposition

D Factorization of Transfer Functions into Minimum Phase Stable and All‐Pass Parts

D.1 Input Factorization of RHP Zeros

D.2 Output Factorization of RHP Zeros

D.3 Output Factorization of RHP Poles

D.4 Input Factorization of RHP Poles

D.5 SISO Systems

D.6 Factoring Out Both RHP Poles and RHP Zeros

Reference

E Models Used in Examples

E.1 Binary Distillation Column Model

E.2 Fluid Catalytic Cracker Model

References

Note

Index

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Tags: Morten Hovd, Advanced Chemical, Process Control