Perkins Interactions Between Process Design and Process Control

1. Auflage 2014
ISBN: 978-1-4832-9790-3
Verlag: Elsevier Science & Techn.
Format: PDF
Kopierschutz: 1 - PDF Watermark

E-Book, Englisch, 241 Seiten, Web PDF

Reihe: IFAC Postprint Volume

The volume provides the systems engineer working in process control, with state-of-the-art research papers and practical applications, which will be a valuable reference source.

Autoren/Hrsg.

Perkins, J. D.

Inhaltsverzeichnis

1;Front Cover;1
2;Interactions between Process Design and Process Control
;2
3;Copyright Page;3
4;Table of Contents;6
5;FOREWORD;10
6;Chapter 1. Effect of Design on the Controllability of Chemical Plants;12
6.1;1 Introduction;12
6.2;2 Process Synthesis and Controllability;14
6.3;3 Controllability evaluation based on steady-state models;15
6.4;4 Controllability evaluation based on linear dynamic models;15
6.5;5 Controllability evaluation based on nonlinear dynamic models;18
6.6;6 Synthesis;19
6.7;7 Conclusions;20
6.8;References;21
7;Chapter 2. EARLY INTEGRATION OF PROCESS AND CONTROL DESIGN;26
7.1;SUMMARY;26
7.2;1. INTRODUCTION;26
7.3;2. STEPS IN INTEGRATED PROCESS AND CONTROL DESIGN;26
7.4;3. CHOICE OF CONTROLLED AND CORRECTING VARIABLES;27
7.5;4. STABILITY AND CONTROLLABILITY ANALYSIS;28
7.6;5. OPTIMUM OPERATING POINTS;29
7.7;6. CONTROL SYSTEM DESIGN;29
7.8;7. ASSESSING CONTROL PERFORMANCE;30
7.9;8. PROS AND CONS OF WORKING IN THE FREQUENCY DOMAIN;30
7.10;9. CONCLUSIONS;31
7.11;ACKNOWLEDGMENT;31
7.12;REFERENCES;31
8;Chapter 3. CONTROLLABILITY MEASURES FOR DISTURBANCE REJECTION;32
8.1;1 Introduction;32
8.2;2 Preliminaries;32
8.3;3 Existing controllability measures;33
8.4;4 Scaling;34
8.5;5 Results on disturbance measures;34
8.6;6 Example: LV-Distillation.;36
8.7;7 Discussion and Conclusion;37
8.8;References;38
9;Chapter 4. Design and Operability of an Energy Integrated Distillation Column;40
9.1;Introduction;40
9.2;2. Operability issues of integrated plants.;41
9.3;3. Plant Description;41
9.4;4. Stability and operability of the plant;42
9.5;5. Modelling of the energy integrated plant;43
9.6;6. Steady state operation of plant;43
9.7;7. Controllability properties of the plant;44
9.8;8. Experimental results;47
9.9;Conclusion;48
9.10;Literature;48
10;Chapter 5. DESIGN MODIFICATIONS AND PROPER DISTILLATION CONTROL;50
10.1;INTRODUCTION;50
10.2;CONTROL STRUCTURES;50
10.3;IMPLICATION OF THE EIGENSTRUCTURE CONCEPT;51
10.4;ALTERNATIVE & HEAT INTEGRATED DISTILLATION CONFIGURATIONS;52
10.5;PROCEDURE FOR CONTROL SYSTEM DESIGN;54
10.6;CONCLUSIONS;54
10.7;REFERENCES;54
11;Chapter 6. Controllability Analysis for Unstable Processes;58
11.1;1 Introduction;58
11.2;2 Controllability measures;58
11.3;3 Examples.;61
11.4;References;63
12;Chapter 7. CONTROL SYSTEM DESIGN IN DISTILLATION PROCESSES AND ITS DEPENDENCE OF THE ORIGINAL PROCESS DESIGN;64
12.1;1 Introduction;64
12.2;2 System Description;65
12.3;3 Discussion;67
12.4;References;72
13;Chapter 8. Design and Control of Recycle Processes in Ternary Systems with Consecutive Reactions;74
13.1;Introduction;74
13.2;Process Studied;75
13.3;Dynamics and Control;76
13.4;A Proposed Generic Rule for Liquid Recycle Systems;78
13.5;Conclusion;79
13.6;Literature Cited;79
13.7;Nomenclature;79
14;Chapter 9. SIMULTANEOUS PROCESS AND SYSTEM CONTROL DESIGN: AN ACTUAL INDUSTRIAL CASE;84
14.1;INTRODUCTION;85
14.2;MODELLING;86
14.3;RESULTS AND DISCUSSION;86
14.4;LITERATURE REFERENCES;92
15;Chapter 10. Concurrent Integrated Design of Process and Operating System;96
15.1;1 Introduction;96
15.2;2 Classifying Modes of Process Operation;96
15.3;3 Defining the Full Operating Regime;97
15.4;4 Functional Structure of Operating Modes;97
15.5;5 Development of Operating Modes;99
15.6;6 Negotiation between Process and Operating System Design;101
15.7;7 Conclusions;101
15.8;References;101
16;Chapter 11. INCORPORATING OPERABILITY MEASURES INTO TEE PROCESS SYNTHESIS STAGE OF DESIGN;104
16.1;PROCESS SYNTHESIS PROCEDURE;104
16.2;SYNTHESIS OF A STYRENE MONOMER FLOWSHEET;106
16.3;CONCLUSIONS;108
16.4;REFERENCES;108
17;Chapter 12. A Multiobjective Optimization Approach For Analyzing The Interaction of Design and Control;110
17.1;1. Process Synthesis and Controllability;110
17.2;2. Multiobjective Optimization Framework;111
17.3;3. Proposed Procedure For Design and Control;113
17.4;4. Two-Objective Example Problem;113
18;Chapter 13. Integrated Design of Effluent Treatment Systems;116
18.1;1 Summary;116
18.2;2 Introduction;116
18.3;3 Analysis of delay effects;116
18.4;4 Worst case design;118
18.5;5 An example from effluent treatment;119
18.6;6 Conclusions;121
18.7;References;121
19;Chapter 14. INTERACTIONS BETWEEN DESIGN AND OPERATION OF BATCH PLANTS;122
19.1;ABSTRACT;122
19.2;KEYWORDS;122
19.3;INTRODUCHON;122
19.4;DESIGN AND DYNAMICS - BATCH DISTILLATION;122
19.5;DESIGN AND SCHEDULING - MULTIPURPOSE BATCH PLANTS;124
19.6;DESIGN OF OPERATING PROCEDURES AND SEQUENTIAL CONTROLLERS;126
19.7;DISCUSSION AND CONCLUSIONS;130
19.8;ACKNOWLEDGEMENTS;130
19.9;REFERENCES;131
20;Chapter 15. A PROCEDURE FOR CONTROLLABILITY ANALYSIS;136
20.1;1 Introduction;136
20.2;2 Control objectives and limitations;136
20.3;3 Scaling of variables;137
20.4;4 Tools for controllability analysis;137
20.5;5 More detailed analysis.;140
20.6;6 Example: FCC;140
20.7;References;141
21;Chapter 16. Is the Relative Gain Array a Sensitivity Measure ?;142
21.1;I Introduction;142
21.2;II Notation and Preliminaries;143
21.3;III Main Results;144
21.4;IV Conclusion;146
21.5;Acknowlegement;146
21.6;References;146
22;Chapter 17. ROBUST CONTROL INDICATORS IN PROCESS DESIGN AND CONTROL;148
22.1;INTRODUCTION;148
22.2;FRAMEWORK FOR TRADE-OFF BETWEEN CRITERIA;148
22.3;ILLUSTRATIVE EXAMPLE;150
22.4;INTEGRATION OF PROCESS DESIGN AND CONTROL;151
22.5;REFERENCES;151
23;Chaper 18. EARLY STAGE PROCESS CONTROLLABILITY ASSESSMENT;154
23.1;1. INTRODUCTION;154
23.2;2. THE REQUIREMENTS OF A CONTROLLABILITY ASSESSMENT TOOL;154
23.3;3 REALISATION OF A PROCESS CONTROL TOOLBOX;155
23.4;4 APPLICATION TO A VINYL CHLORIDE PLANT;156
23.5;5 APPLICATION TO A POLYMERISATION REACTOR;157
23.6;6 SUMMARY;158
23.7;7 REFERENCES;158
24;Chapter 19. Inferential Control using Nonlinear Model-based Observer Control;160
24.1;1 Introduction;160
24.2;2 The Flash Separation Process;160
24.3;3 The Control Structure Assessment;161
24.4;4 Model-Based Observer Control;162
24.5;5 Inferential Control of the Flash Separation;163
24.6;6 Discussion and Conclusions;165
24.7;7 References;165
25;Chapter 20. CONTROL CONFIGURATION SELECTION FOR THE INFERENTIAL CONTROL OF A HIGH PURITY DISTILLATION COLUMN;166
25.1;INTRODUCTION;167
25.2;INDUSTRIAL DISTILLATION COLUMN;167
25.3;EIGENSTRUCTURE STUDIES;169
25.4;CONCLUSION;171
26;Chapter 21. THE MODEL PROJECTION PROBLEMS IN THE GLOBAL INSTRUMENTATION OF A PROCESS;176
26.1;1 INTRODUCTION: PROBLEM MOTIVATION;176
26.2;2 PROGENITOR MODELS AND PROBLEM STATEMENT;176
26.3;3 INTERNAL PROGENITOR MODELS AND THEIR PROPERTIES UNDER TOTAL LOSS OF SUBSYSTEM INPUTS, OUTPUTS;177
26.4;4 MODEL PROJECTION PROBLEMS ON EXTERNAL PROGENITOR MODELS;178
26.5;5 CONCLUSIONS;179
26.6;References;179
27;Chapter 22. COMPUTER-AIDED OPTIMAL DYNAMIC NETWORK DESIGN;180
27.1;ABSTRACT;180
27.2;INTRODUCnON;180
27.3;THE ALGORITHMS OF THE SOLUTION OF THE NETWORK DESIGN PROBLEMS;182
27.4;THE ARCHITECTURE OF THE AUTOMATIZED SYSTEM;184
27.5;THE INTERACTION BETWEEN PROCESS CONTROL AND PROCESS DESIGN;185
27.6;REFERENCES;185
28;Chapter 23. OPTIMAL DESIGN AND OPERATION OF COMPLEX BATCH DISTILLATION COLUMN;186
28.1;Introduction;186
28.2;Complex Batch Distillation Column;186
28.3;Optimal Design and Operation of Complex Column;187
28.4;Stripping Batch Distillation Column;188
28.5;Conclusion;191
28.6;Acknowledgment;191
29;Chaper 24. Dynamic Modeling in Design and Operation Safety Checking of Large Scale Pipeline Networks;192
29.1;Introduction;192
29.2;1) Process design and operation;192
29.3;2) Operability and controllability studies;194
29.4;3) Optimization of process design and operation - simulation runs under user defined logic;195
29.5;4) Design and control for inherent safety - leak detection;196
29.6;Conclusions;197
29.7;References;197
30;Chapter 25. COMPUTER-AIDED PROCESS DESIGN SYSTEM FOR PLANT OPERATION;198
30.1;1 INTRODUCTION;199
30.2;2. DESIGN ACTIVITIES FOR START-UP;199
30.3;3. CORRESPONDENCE BETWEEN TOPOLOGY AND START-UP OPERATION;200
30.4;4. PROCESS DESIGN SUPPORT SYSTEM FOR OPERATION;202
30.5;5. CONCLUSION;203
31;Chapter 26. COMPARISON OF SEVERAL STARTUP MODELS FOR BINARY AND TERNARY BATCH DISTILLATION WITH HOLDUPS;206
31.1;INTRODUCTION;206
31.2;STARTUP MODELS AND SIMULATION ASPECTS;207
31.3;SIMULATION RESULTS AND DISCUSSION;207
31.4;CONCLUSION;209
31.5;ACKNOWLEDGMENT;209
31.6;REFERENCE;209
32;Chapter 27. The Desiyn and Scheduling of Multipurpose Batch Plants;212
32.1;1 Introduction;212
32.2;2 Problem Definition and Formulation;213
32.3;3 An Example;215
32.4;4 Conclusions;216
32.5;References;217
33;Chapter 28. Supervisory Control of Parallel Processes in Batch Plants;218
33.1;Problem;218
33.2;Causal Models;218
33.3;Timed Models;219
33.4;Analysis of Timed Models;220
33.5;Application;222
33.6;Acknowledgement;223
33.7;References;223
34;Chapter 29. A Knowledge-Based Expert System for Hazard and Operability Studies;224
34.1;1. Introduction;224
34.2;2. Hazard and Operability (HAZOP) Study and Needs for Expert System;224
34.3;3. Knowledge Representation and System Implementation;225
34.4;4. Examples;227
34.5;5. Conclusion and Further Studies;229
34.6;References;229
35;Chapter 30. COMPUTER EMULATION OF HAZARD IDENTIFICATION;230
35.1;1. Introduction;230
35.2;2. Hazop Procedure;230
35.3;3. The HAZID Knowledge Based System;231
35.4;4. Discussion;234
35.5;5. Applications;234
35.6;6. Current status;235
35.7;7. Conclusion;235
35.8;Acknowledgments;235
35.9;References;235
36;Chapter 31. A Hierarchical Method for Line-by-Line Hazard and Operability Studies;236
36.1;Introduction: the Line-by-Line Hazard Study Method;236
36.2;Hierarchical Approach to Process Design Tasks;237
36.3;A Hierarchical Line-by-Line Hazop Case Study;238
36.4;The Process Example;238
36.5;Input - Output Block Flow Diagram;239
36.6;Input-Output BFD with Controls;239
36.7;Recycle BFD;240
36.8;Unintegrated Process Flowsheet;240
36.9;Conclusions;241
36.10;References;242
37;Chapter 32. Design of Flexible and Reliable Process Systems;244
37.1;1. INTRODUCTION;244
37.2;2. PROBLEM DEFINITION;244
37.3;3. FRAMEWORK;245
37.4;4. EXAMPLE;245
37.5;5. CONCLUSIONS;248
37.6;6. REFERENCES;248
38;APPENDIX;249