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9783540792239

Diagnosis of Process Nonlinearities and Valve Stiction

by ; ;
  • ISBN13:

    9783540792239

  • ISBN10:

    3540792236

  • Format: Hardcover
  • Copyright: 2008-11-13
  • Publisher: Springer Nature
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List Price: $219.99

Summary

The subject matter of the book is concerned with the detection and diagnosis of process nonlinearities from routine process data. In general, processes can be treated as locally linear and measures of overall process performance can be monitored from routine operating data. However when process performance is not satisfactory then it is imperative that the cause of poor performance be diagnosed. Poor performance can be due to several reasons. Statistics abound on the cause of poor control performance. It has been documented that as many as 40% of the control loops in industry perform unsatisfactorily because of valve problems, a majority of them due to valve stiction, causing the closed loop system to become nonlinear. The development of signal processing methods to detect and quantify process nonlinearity from routine process data is the main subject matter of this book.

Author Biography

M. A. A. Shoukat Choudhury received his B. Sc. Engineering (Chemical) from Bangladesh University of Engineering and Technology (BUET), Dhaka, Bangladesh in 1996. He was awarded a gold medal for his outstanding results in B. Sc. Engineering. He obtained an M. Sc. Engineering (Chemical) in 1998 from the same university. He has completed his PhD degree in process control (Chemical Engineering) at the University of Alberta, Canada. For his outstanding research performance during the course of PhD program he has been awarded several awards such as University of Alberta PhD Dissertation Fellowship, Andrew Stewart Memorial Prize and ISA Educational Foundation Scholarship. He is the principal inventor of an internation patent (applied, 2005) on "Methods for Detection and Quantification of Control Valve Stiction". The methodologies and algorithms described in this patent are implemented and available in the commercial software ProcessDoctor from Matrikon Inc. His main research interests include diagnosis of poor control performance, stiction in control valves, data compression, control loop performance assessment and monitoring, and diagnosis of plant wide oscillations.Sirish Shah received his B.Sc. degree in control engineering from Leeds University in 1971, a M.Sc. degree in automatic control from UMIST, Manchester in 1972, and a Ph.D. degree in process control (chemical engineering) from the University of Alberta in 1976. During 1977 he worked as a computer applications engineer at Esso Chemicals in Sarnia, Ontario. Since 1978 he has been with the University of Alberta, where currently holds the NSERC-Matrikon-ASRA Senior Industrial Research Chair in Computer Process Control. In 1989, he was the recipient of the Albright & Wilson Americas Award of the Canadian Society for Chemical Engineering in recognition of distinguished contributions to chemical engineering. He has held visiting appointments at Oxford University and Balliol College as a SERC fellow in 1985-86 and at Kumamoto University, Japan as a senior research fellow of the Japan Society for the Promotion of Science (JSPS) in 1994. The main area of his current research is process and performance monitoring, system identification and design and implementation of softsensors. He has recently co-authored a book titled, Performance Assessment of Control Loops: Theory and Applications. He has held consulting appointments with a wide variety of process Industries and has also taught many industrial courses.

Table of Contents

Introductionp. 1
Concepts in Data-Driven Analysis of Chemical Processesp. 2
Linear and Nonlinear Time Seriesp. 3
Statistics and Randomnessp. 3
Frequency Content and Spectral Methodsp. 6
Nonlinearity in Control Valvesp. 8
The Layout of the Bookp. 10
Part I Higher-Order Statisticsp. 10
Part II Data Quality - Compression and Quantizationp. 10
Part III Nonlinearity and Control Performancep. 11
Part IV Control Valve Stiction - Definition, Modelling, Detection and Quantificationp. 12
Part V Plant-wide Oscillations - Detection and Diagnosisp. 13
Referencesp. 14
Summaryp. 14
Higher-Order Statistics
Higher-Order Statistics: Preliminariesp. 17
Introductionp. 17
Time Domain Analysisp. 18
Momentsp. 18
Cumulantsp. 20
The Relationship Between Moments and Cumulantsp. 22
Properties of Moments and Cumulantsp. 22
Moments and Cumulants of Stationary Signalsp. 25
Spectral Analysisp. 25
Power Spectrum, n=2p. 26
Bispectrum, n=3p. 27
Summaryp. 28
Bispectrum and Biocherencep. 29
Bispectrump. 29
Estimation of the Bispectrump. 30
Properties of Estimators and Asymptotic Behaviourp. 32
Bicoherence or Normalized Bispectrump. 34
Properties of Bispectrum and Bicoherencep. 35
Bispectrum or Bicoherence Estimation Issuesp. 37
Choice of Window Functionp. 38
Choice of Data Length, Segment Length and Fourier Transform Lengthp. 40
Summaryp. 41
Data Quality - Compression and Quantization
Impact of Data Compression and Quantization on Data-Driven Process Analysesp. 45
Introductionp. 45
Data Compression Methodsp. 47
Overview of Data Compressionp. 47
Box-Car (BC) Algorithmp. 47
Backward-Slope (BS) Algorithmp. 47
Combined Box-Car and Backward-Slope (BCBS) Methodp. 49
Swinging Door Compression Algorithmp. 49
The Compression Factorp. 49
Measures of Data Qualityp. 50
Statistical Measuresp. 50
Nonlinearity Measuresp. 51
Performance Index (Harris) Measuresp. 51
Process Data for Compression Comparisonp. 52
Industrial Example 1p. 52
Industrial Example 2p. 55
Results and Discussions for Industrial Example 2p. 56
Visual Observationsp. 56
Statistical Propertiesp. 57
Nonlinearity Assessmentp. 58
Performance (Harris) Indexp. 58
Summary of Data Quality Measuresp. 59
Automated Detection of Compressionp. 59
Motivationp. 59
Compression Detection Procedurep. 60
Implementation Considerationsp. 61
A Recommendation for Harmless Storing of Datap. 63
Quantizationp. 63
Summaryp. 65
Nonlinearity and Control Performance
Measures of Nonlinearity - A Reviewp. 69
Definition of Nonlinear Systemsp. 69
Nonlinearity in Process Time Trendsp. 70
Various Measures of Nonlinearityp. 70
Model-Based Measures of Nonlinearityp. 71
Time Series-Based Measures of Nonlinearityp. 71
Summaryp. 75
Linear or Nonlinear? A Bicoherence-Based Measure of Nonlinearityp. 77
Introductionp. 77
Bispectrum and Biocherencep. 78
Spurious Peaks in the Estimated Bicoherencep. 78
Illustrative Example 1p. 79
How to Choose [epsilon]?p. 80
Test of Gaussianity and Linearity of a Signalp. 81
Total Nonlinearity Index (TNLI)p. 85
Illustrative Example 2: Bicoherence of a Linear and a Nonlinear Signalp. 85
Illustrative Example 3: Bicoherence of a Nonlinear Sinusoid Signal with Noisep. 87
Mild Nonlinearity (n[subscript l] = 0.05)p. 88
Strong Nonlinearity (n[subscript l] = 0.25)p. 89
Extent of Nonlinearity and Effect of Noisep. 90
Summaryp. 91
A Nonlinearity Measure Based on Surrogate Data Analysisp. 93
Surrogate Time Seriesp. 93
Nonlinearity Detection Using Surrogatesp. 93
Predictability in Nonlinear Time Seriesp. 93
Algorithm for Nonlinearity Diagnosisp. 95
Construction of the Data Matrix for Nonlinear Predictionp. 95
Calculation of Prediction Errorp. 96
Calculation of Surrogate Datap. 96
Statistical Testingp. 98
Algorithm Summaryp. 98
Selection of the Parameter Valuesp. 99
Recommended Default Parameter Valuesp. 99
Choice of Embedding Parameters E and Hp. 99
Choice of Parameters C and kp. 100
Default Data Ensemble Size, Q and Number of Samples Per Feature, Sp. 101
Choice of the Number of Surrogates, Mp. 101
Data-Preprocessing and End-Matchingp. 102
False-Positive Results with Cyclic Datap. 102
End-Matchingp. 103
Summary of the Data-Preprocessing Stepsp. 104
Application to Oscillating Time Grendsp. 104
Worked Examplesp. 106
Identification of Nonlinear Root Causesp. 106
Application to the SE Asia Data Setp. 106
The Mechanisms of Propagation in the SE Asia Processp. 106
An Example with No Nonlinearityp. 108
Summaryp. 110
Nonlinearities in Control Loopsp. 111
Process Nonlinearityp. 111
Nonlinearity of a Spherical Tankp. 111
Nonlinearities of a Continuous Stirred Tank Reactor (CSTR)p. 115
Nonlinear Valve Characteristicp. 117
Linear Valvesp. 118
Equal Percentage Valvesp. 118
Square-Root Valvep. 119
Remarks on Nonlinear Valve Characteristicp. 120
Nonlinear Disturbancesp. 121
Summaryp. 121
Diagnosis of Poor Control Performancep. 123
Introductionp. 123
Problem Descriptionp. 124
Usual Causes of Poor Performancep. 125
Diagnosis of Poor Control Performancep. 126
Well Tuned Controllerp. 127
Tightly Tuned Controller or Excessive Integral Actionp. 128
Presence of an External Oscillatory Disturbancep. 129
Presence of Stictionp. 129
Industrial Case Studiesp. 129
Stiction in a Furnace Dryer Temperature Control Valvep. 130
Valve Saturationp. 131
Valve Problems in Some Flow Control Loopsp. 132
Summaryp. 134
Control Valve Stiction - Definition, Modelling, Detection and Quantification
Different Types of Faults in Control Valvesp. 137
What Is a Control Valvep. 137
Faults in Control Valvep. 138
Oversized Valvep. 139
Undersized Valvep. 139
Corroded Valve Seatp. 139
Faulty Diaphragmp. 139
Packing Leakagep. 139
Valve Hysteresisp. 140
Valve Stictionp. 140
Large Deadbandp. 140
Valve Saturationp. 141
Summaryp. 141
Stiction: Definition and Discussionsp. 143
Introductionp. 143
What Is Stiction?p. 143
Definition of Terms Relating to Valve Nonlinearityp. 144
Discussion of the Term 'Stiction'p. 145
A Formal Definition of Stictionp. 146
Practical Examples of Valve Stictionp. 148
Summaryp. 151
Physics-Based Model of Control Valve Stictionp. 153
Introductionp. 153
Physical Modelling of Valve Frictionp. 153
Physics of a Control Valvep. 153
Friction Modelp. 154
Model Parametersp. 155
Detection of Zero Velocityp. 156
Model of the Pressure Chamberp. 156
Valve Simulationp. 157
Open-Loop Responsep. 157
Closed-Loop Responsep. 158
Summaryp. 160
Data-Driven Model of Valve Stictionp. 161
One-Parameter Data-Driven Stiction Modelp. 161
Two-Parameter Data-Driven Model of Valve Stictionp. 163
Model Formulationp. 163
Dealing with Stochastic or Noisy Control Signalsp. 166
Open-Loop Response of the Model Under a Sinusoidal Inputp. 166
Stiction in Realityp. 167
Closed-Loop Behaviour of the Modelp. 167
Comparison of Physics-Based Model and Data-Driven Modelp. 171
Summaryp. 171
Describing Function Analysisp. 173
Introductionp. 173
Describing Function Analysis for Two-Parameter Stiction Modelp. 174
Derivation of the Describing Functionp. 174
Asymptotes of the Describing Functionp. 177
Insights Gained from the Describing Functionp. 178
The Impact of the Controller on the Limit Cyclep. 179
Summaryp. 180
Automatic Detection and Quantification of Valve Stictionp. 181
Introductionp. 181
Stiction Detection - A Literature Reviewp. 182
Detection of Stiction Using Nonlinearity Information and the pv-op Mappingp. 183
Detection of Loop Nonlinearityp. 184
Use of pv-op Plotp. 185
Stiction Quantificationp. 187
Clustering Techniques of Quantifying Stictionp. 187
Fitted Ellipse Technique for Quantifying Stictionp. 190
An Illustrative Examplep. 192
Validation of the Resultsp. 193
Automation of the Methodp. 193
Simulation Resultsp. 195
A Worked Examplep. 195
Distinguishing Limit Cycles Caused by Stiction and Those Caused by a Sinusoidal Disturbancep. 196
Detecting Stiction When Its Impact Propagates as Disturbancep. 198
Practical Implementation Issuesp. 201
Bicoherence Estimationp. 201
Nonstationarity of the Datap. 201
Problems of Outliers and Abrupt Changesp. 201
Dealing with Short Length Datap. 202
Dealing with Longer Oscillationsp. 202
Valve Nonlinearityp. 202
Filtering of the Datap. 203
Segmenting Data for pv-op Plotp. 204
Summaryp. 204
Industrial Applications of the Stiction Quantification Algorithmp. 205
Industrial Case Studiesp. 205
Loop 1: A Level Loopp. 205
Loop 2: A Linear-Level Control Loopp. 207
Loop 3: A Flow Control Loopp. 208
Loop 4: Flow Control Loop Cascaded with Level Controlp. 209
Loop 5: A Pressure Control Loopp. 210
Loop 6: A Composition Control Loopp. 210
Loop 7: A Cascaded Flow Control Loopp. 211
Loop 8: A Temperature Control Loopp. 212
Loops 9 and 10p. 212
Online Compensation for Stictionp. 213
Summaryp. 215
Confirming Valve Stictionp. 217
Methods to Confirm Valve Stictionp. 217
Gain Change Method for Confirming Valve Stictionp. 218
Distinguishing Stiction from External Oscillatory Disturbancep. 218
Describing Function Analysisp. 222
Comparison of Describing Function Analysis (DFA) Results with Simulation Resultsp. 225
Industrial Examplep. 225
Summaryp. 226
Plant-wide Oscillations - Detection and Diagnosis
Detection of Plantwide Oscillationsp. 229
Introductionp. 229
What is an Oscillation?p. 230
Units of Frequencyp. 230
Examples of Oscillatory Signalsp. 230
Detection of Oscillation(s) in a Single Time Seriesp. 231
The Power Spectrump. 231
Hagglund's IAE Methodp. 231
Autocovariance (ACF) Based Methodp. 232
Other Methodsp. 237
What are Plant-wide Oscillations?p. 237
Classification of Plant-wide Oscillations or Disturbancesp. 237
Time scalesp. 237
Oscillating and Non-oscillating Disturbancesp. 238
Detection of Plant-wide Oscillationsp. 238
High-Density Plotsp. 238
ACF-Based Methodp. 239
Power Spectral Correlation Map (PSCMAP)p. 239
Spectral Envelope Methodp. 240
Spectral Decomposition Methodsp. 241
Summaryp. 250
Diagnosis of Plant-wide Oscillationsp. 253
Root Cause Diagnosis of Plant-wide Oscillationp. 253
Finding a Nonlinear Root Cause of a Plant-Wide Disturbancep. 253
Finding a Linear Root Cause of a Plant-wide Disturbancep. 256
Industrial Case Study 1 - Eastman Chemical Plantp. 257
Data Descriptionp. 258
Reduction of the Problem Sizep. 258
Detection of Plant-wide Oscillation by PSCMAPp. 259
Nonlinearity Analysis Using Biocherence-Based Indicesp. 260
Diagnosis of the Problem in Loop LC2p. 262
Industrial Case Study 2 - SE Asia Refinery Data Analysisp. 263
Oscillation Detection by PSCMAPp. 264
Oscillation Detection by Spectral Envelopep. 265
Oscillation Diagnosisp. 266
Industrial Case Study 3 - Mitshubishi Chemical Corporationp. 266
Scope of the Analysis and Data Setp. 268
Oscillation-Detection Resultsp. 268
Oscillation Diagnosisp. 268
The Results of Maintenance on the PC1 and LI1 Loopsp. 271
Summaryp. 272
Referencesp. 273
Copyright Acknowledgementsp. 281
Indexp. 283
Table of Contents provided by Ingram. All Rights Reserved.

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