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FAULT DETECTION AND DIAGNOSIS VIA
IMPROVED MULTIVARIATE STATISTICAL PROCESS CONTROL
NOORLISA BINTI HARUN
UNIVERSITI TEKNOLOGI MALAYSIA
FAULT DETECTION AND DIAGNOSIS VIA
IMPROVED MULTIVARIATE STATISTICAL PROCESS CONTROL
NOORLISA BINTI HARUN
A thesis submitted in fulfilment of the
requirements for the award of the degree of
Master of Engineering (Chemical)
Faculty of Chemical and Natural Resources Engineering
Universiti Teknologi Malaysia
JULY 2005
iii
In the Name of Allah, Most Gracious, Most Merciful.
I humbly dedicate to…
my beloved family members
my best friend
those who has shaped my life and
those who has influenced my life on the right path.
iv
ACKNOWLEDGEMENT
Firstly, I would like to take this opportunity to thank my respectful
supervisor, Assoc. Prof. Dr. Kamarul Asri Ibrahim who has relentlessly given
guidance, constructive ideas and invaluable advice, enabling me to achieve the
objective of this dissertation. In addition I am very grateful to my family members,
no amount of gratitude could repay their kindness of being there as well as the
patience to put up with my whim.
I also would like to thank my fellow course mates and friends for the
assistances, advices and ideas in producing a resourceful, fruitful and practicable
research. May God bless all of you.
v
ABSTRACT
Multivariate Statistical Process Control (MSPC) technique has been widely
used for fault detection and diagnosis (FDD). Currently, contribution plots are used
as basic tools for fault diagnosis in MSPC approaches. This plot does not exactly
diagnose the fault, it just provides greater insight into possible causes and thereby
narrow down the search. Hence, the cause of the faults cannot be found in a
straightforward manner. Therefore, this study is conducted to introduce a new
approach for detecting and diagnosing fault via correlation technique. The correlation
coefficient is determined using multivariate analysis techniques, namely Principal
Component Analysis (PCA) and Partial Correlation Analysis (PCorrA). An industrial
precut multicomponent distillation column is used as a unit operation in this research.
The column model is developed using Matlab 6.1. Individual charting technique such
as Shewhart, Exponential Weight Moving Average (EWMA) and Moving Average
and Moving Range (MAMR) charts are used to facilitate the FDD. Based on the
results obtained from this study, the efficiency of Shewhart chart in detecting faults
for both quality variables (Oleic acid, xc8 and linoleic acid, xc9) are 100%, which is
better than EWMA (75% for xc8 and 77.5% for xc9) and MAMR (63.8% for xc8 and
70% for xc9). The percentage of exact faults diagnoses using PCorrA technique in
developing the control limits for Shewhart chart is 100% while using PCA is 87.5%.
It shows that the implementation of PCorrA technique is better than PCA technique.
Therefore, the usage of PCorrA technique in Shewhart chart for fault detection and
diagnosis gives the best for it has the highest fault detection and diagnosis efficiency.
vi
ABSTRAK
Proses Kawalan Statistik Multipembolehubah (MSPC) digunakan secara
meluas untuk mengesan dan mengenalpasti punca kesilapan. Pada masa kini, carta
penyumbang digunakan untuk mengenalpasti punca kesilapan dalam MSPC. Carta
ini tidak dapat mengenalpasti punca kesilapan dengan tepat yang mana ia sekadar
menunjukkan kemungkinan besar punca kesilapan dan membantu memudahkan
pencarian punca kesilapan. Oleh itu, punca kesilapan tidak dapat ditentukan secara
langsung. Justeru, kajian ini telah dijalankan bagi memperkenalkan satu pendekatan
baru untuk mengesan dan mengenalpasti punca kesilapan melalui teknik korelasi.
Pekali korelasi ditentukan melalui kaedah Analisis Statistik Multipembolehubah iaitu
Analisis Komponen Utama (PCA) dan Analisis Korelasi Separa (PCorrA). Turus
penyulingan multikomponen industri digunakan sebagai operasi unit. Model turus ini
dibangunkan menggunakan perisian Matlab 6.1. Teknik carta individu yang terdiri
daripada Shewhart, Exponential Weight Moving Average (EWMA), dan Moving
Average dan Moving Range (MAMR) digunakan bagi mengesan dan mengenalpasti
punca kesilapan. Berdasarkan kepada keputusan yang diperolehi, kecekapan carta
Shewhart dalam mengesan kesilapan untuk kedua-dua pembolehubah kualiti (Asid
oliek, xc8 dan asid linoleik, xc9) adalah 100% yang mana lebih baik berbanding
dengan carta EWMA (75% bagi xc8 and 77.5% bagi xc9)dan carta MAMR (63.8% bagi
xc8 and 70% bagi xc9). Peratusan mengenalpasti punca kesilapan secara tepat
menggunakan teknik PCorrA bagi carta Shewhart adalah 100% manakala PCA
adalah 87.5%. Ini menunjukkan bahawa penggunaan teknik PCorrA adalah lebih
baik berbanding teknik PCA. Oleh itu, penggunaan teknik PCorrA dalam carta
Shewhart bagi tujuan mengesan dan mengenalpasti punca kesilapan adalah yang
terbaik dengan peratusan kecekapan yang paling tinggi.
vii
TABLE OF CONTENTS
CHAPTER TITLE PAGE
TITLE PAGE i
DECLARATION ii
DEDICATION iii
ACKNOWLEDGEMENT iv
ABSTRACT v
ABSTRAK vi
TABLE OF CONTENTS vii
LIST OF TABLES xii
LIST OF FIGURES xiv
LIST OF SYMBOLS xvi
LIST OF ABBREVIATIONS xx
LIST OF APPENDICES xxi
1 INTRODUCTION
1.1 Introduction 1
1.2 Research Background 2
1.3 Objectives of the Research 4
1.4 Scopes of the Research 4
1.5 Contributions of the research 5
1.6 Chapter Summary 5
viii
2 LITERATURE REVIEW
2.1 Introduction 7
2.2 Definitions of Fault, Fault Detection and Fault Diagnosis 8
2.3 Multivariate Statistical Analysis, MSA 9
2.4 Review on Principal Component Analysis, PCA 10
2.4.1 Extension of Principal Component Analysis, PCA
method
2.4.1.1 Multi-Way PCA 14
2.4.1.2 Multi-Block PCA 15
2.4.1.3 Moving PCA 16
2.4.1.4 Dissimilarity, DISSIM 17
2.4.1.5 Multi-Scale PCA 18
2.4.2 PCA Adopted in Industries 19
2.4.3 PCA as Controller 20
2.4.4 Theory of PCA 21
2.5 Review on Partial Correlation Analysis, PCorrA 23
2.5.1 Theory of PCorrA 26
2.6 Chapter Summary 27
3 IMPROVED STATISTICAL PROCESS CONTROL CHART
3.1 Statistical Process Control, SPC 29
3.2 Traditional Statistical Process Control, SPC chart 30
3.2.1 Shewhart Chart 31
3.2.2 Exponential Weight Moving Average, EWMA Chart 35
3.2.3 Moving Average and Moving Range, MAMR Chart 39
3.3 Improve Statistical Process Control Chart 43
3.4 Chapter Summary 45
ix
4 DYNAMIC SIMULATED DISTILLATION COLUMN
4.1 Introduction 46
4.2 Process Description of Precut Column 48
4.3 The Information of Pre-cut column 49
4.4 Degree of Freedom (DoF) Analysis 51
4.5 Formulations of the Distillation Column Models 56
4.5.1 Mass Balance Equations 56
4.5.1.1 Bottom column model 58
4.5.1.2 Trays model 59
4.5.1.3 Reflux drum model 61
4.5.1.4 Pumparound drum model 62
4.5.2 Equilibrium Equations 63
4.5.2.1 Bubble Point Calculations 66
4.5.3 Summation Equation 68
4.5.4 Heat Balance Equation 68
4.5.5 Hydraulic Equations 69
4.6 Dynamic Simulation of the Study Column 70
4.7 Controller Tuning 74
4.7.1 Bottom Liquid Level Controller 75
4.7.2 Bottom Temperature Controller 76
4.7.3 Top Column Pressure Controller 78
4.7.4 Sidedraw Tray Liquid Level Controller 79
4.7.5 Pumparound Temperature Controller 80
4.7.6 Pumparound Flow Rate Controller 81
4.7.7 Reflux Flow Rate Controller 82
4.7.8 Controller Sampling Time, TAPC 82
4.8 Dynamic simulation Program Performance Evaluation 83
4.9 Chapter Summary 84
x
5 METHODOLOGY
5.1 Introduction 86
5.2 Variable Selection for Process Monitoring 87
5.3 Statistical Process Control Sampling Time, TSPC 90
5.4 Normal Operating Condition (NOC) Data Selection and
Preparation
92
5.4.1 Data pretreatment 94
5.4.2 Correlation Coefficient via Multivariate Analysis
Techniques
94
5.4.2.1 Principal Component Analysis, PCA 95
5.4.2.2 Partial Correlation Analysis, PCorrA 101
5.4.3 Control limits of Improved Statistical Process
Control, ISPC chart
103
5.5 Generated Out of Control, OC data 105
5.6 Fault Coding Monitoring Framework 109
5.7 Performance Evaluation of the FDD Method 111
5.7.1 Fault Detection Efficiency 111
5.7.2 Fault Diagnosis Efficiency 112
5.8 Chapter Summary 113
6 RESULTS AND DISCUSSIONS
6.1 Statistical Process Control Sampling Time, TSPC 116
6.2 Normal Operating Condition, NOC Data 117
6.2.1 Correlation coefficient via Principal Component
Analysis, PCA
119
6.2.2 Correlation coefficient via Partial Correlation
Analysis, PCorrA
123
6.3 Parameters to Design Improved Statistical Process Control
chart
124
6.4 Fault Detection and Diagnosis Method Performance 127
6.4.1 False alarm Analysis 127
xi
6.4.2 Fault Detection Efficiency Results and Results
Discussions
129
6.4.3 Fault Diagnosis Efficiency Results and Results
Discussions
132
6.5 Chapter Summary 136
7 CONCLUSIONS AND RECOMMENDATIONS
7.1 Introduction 138
7.2 Conclusions of Improved SPC framework 139
7.3 Recommendations to Future Research 141
LIST OF REFERENCES 142
APPENDICES 154
xii
LIST OF TABLES
TABLE NO. TITLE PAGE
4.1 Specification of the pre-cut column 49
4.2 Components composition and conditions of the pre-cut column 50
4.3 Number of variables 52
4.4 Number of equations 53
4.5 Control loops properties 55
4.6 Cohen-Coon controller settings 75
4.7 The step change results for bottom liquid level controller 76
4.8 Properties of bottom liquid level P controller 76
4.9 The step change results for bottom temperature controller 77
4.10 Properties of bottom temperature PID controller 77
4.11 The step change results for top column pressure controller 78
4.12 Properties of top column pressure PI controller 78
4.13 The step change results for sidedraw tray liquid level controller 79
4.14 Properties of sidedraw tray liquid level P controller 79
4.15 The step change results for pumparound temperature controller 80
4.16 Properties of pumparound temperature PID controller 81
4.17 Properties of pumparound flow rate P controller 81
4.18 Properties of reflux flow rate P controller 82
5.1 APC variables for each control loops 87
5.2 Normal correlation coefficient for process variables 88
5.3 SPC variables 88
xiii
5.4 The control limits of Improved SPC chart 104
5.5 Parameters to design EWMA 105
5.6 Description of sensor fault, valve fault and controller fault 107
5.7 Improved SPC chart statistic for FDD 108
5.8 Coding system for fault detection 109
5.9 Coding system for fault diagnosis 109
5.10 Fault coding system for Shewhart Chart 110
5.11 Fault coding system for EWMA Chart 110
5.12 Fault coding system for MAMR Chart 110
6.1 Time constant for each control loops 116
6.2 The skewness and kurtosis value of NOC data 118
6.3 Summary of the NOC data 118
6.4 Eigenvectors Matrix 119
6.5 Eigenvalues, variation explained by each PC and cumulative
variation
119
6.6 The correlation coefficient using different cumulative variation 121
6.7 The percentage difference for two PCs retained and three PCs
retained compared to six PCs
122
6.8 Simple correlation matrix 123
6.9 The correlation coefficient result using PCorrA 124
6.10 Constant to design Shewhart range chart 124
6.11 FDD result using different L and β to design EWMA chart 125
6.12 FDD result using PCA with different window size to design
MAMR chart
126
6.13 FDD result using PCorrA with different window size to design
MAMR chart
126
6.14 False alarm result corresponding to oleic acid composition 128
6.15 False alarm result corresponding to linoleic acid composition 128
6.16 The known fault causes 129
6.17 The known out of control, OC conditions 130
xiv
LIST OF FIGURES
FIGURE NO. TITLE PAGE
2.1 Multi-block PCA monitoring framework 15
3.1 Shewhart range and Shewhart individual chart during normal
condition
34
3.2 Shewhart range and Shewhart individual chart during faulty
condition
34
3.3 EWMA control chart under normal condition 38
3.4 EWMA control chart under faulty condition 38
3.5 Moving average and range control chart under normal condition 42
3.6 Moving average and range control chart under faulty condition 42
3.7 The implementation of correlation coefficient, Cjk in SPC chart 44
4.1 Pre cut column 48
4.2 Distillation column control loop 54
4.3 Distillation column schematic diagram 57
4.4 Bubble point calculation procedure 67
5.1 The procedure to calculate and implement TSPC 92
5.2 Example Scree plot 97
5.3 The procedures to determine correlation coefficient, Cjk via PCA
method
100
5.4 The procedures to determine correlation coefficient, Cjk via
PCorrA metho
103
5.5 The outlined of FDD algorithm
115
xv
6.1 The autocorrelation plot 117
6.2 Histogram plot of NOC data 118
6.3 Scree plot 120
6.4 Fault detection efficiency using different Improved SPC chart 131
6.5 Percentage of faults occurs in different region detected by each
Improved SPC chart
132
6.6 Fault diagnosis situation using PCA for oleic acid composition 133
6.7 Fault diagnosis situation using PCorrA for oleic acid
composition
134
6.8 Fault diagnosis situation using PCA for linoleic acid
composition
134
6.9 Fault diagnosis situation using PCorrA for linoleic acid
composition
135
xvi
LIST OF SYMBOLS
aij - Wilson constant
n - Number of retained principal component
A - Square matrix
Ab - Bottom column area
At - tray active area
Ai,Bi,Ci - Antoine constant for component i
A*,B*,C*,D* - Constant for liquid heat capacity
A2, ,'001.D '
999.D - Constant for MA and MR control limit
β - Weighting factor
B - Bottom flow rate
Cj,k - Correlation coefficient between variable j and variable k
δ - Shifted value in standard deviation unit
D - Distillate flowrate
FDetect - Fault Detection
FDiagnose - Fault Diagnosis
vapH∆ - Heat of vaporization
nvapH ,∆ - Heat of vaporization at normal boiling point
hN - Liquid enthalpy leaving each tray
hb - Enthalpy for bottom stream
how - Over weir height
H, h - CuSum control limits
HN - Vapor enthalpy leaving each tray
xvii
I - Identity matrix
cK - Controller Gain
Kp - Static Gain,
L28 - Liquid flowrate at tray 28
LH, P - Pumparound drum height
Lf - Liquid feed flowrate
LH, Re - Reflux drum liquid level
LH, B - Bottom liquid level
L - Width of the control limit
M - Number of observations
MB - Bottom molar hold-up
MW - Molecular weight
MRe - Reflux drum molar hold-up
MP - Pumparound drum molar hold-up
MN - Molar hold up at tray N
N - Number of stages
p - Number of observations
P - Pumparound flowrate
Pci - Critical pressure of component i sat
iP - Vapor pressure for component i
Ptot - Total pressure of the system
ρ - Liquid density
QR - Reboiler heat duty
Q - Number of variables for response variables
R - Correlation matrix
rj,k - Correlation value between variable j and variable k
Re - Reflux flowrate
R - Universal gas constant
rk - Autocorrelation coefficient
xviii
S - Sidedraw flowrate
S - Variance-Covariance matrix
sj,k - Covariance value of variable j and variable k
s - NOC standard deviation
T - Temperature of the system
Tci - Critical temperature of component i
Tri - Reduced temperature of component i
Tb,i - Boiling point for component i
TAPC - APC sampling time
TSPC - SPC sampling time
t, u - Latent vectors
τ - Time Constant
τD - Derivative Time Constant
τI - Integral Time Constant
θ - Dead time
V - Eigenvector matrix
v - Eigenvector or loading vectors
V - Vapor flowrate
Vci - Critical volume for component i
Vi - Liquid molar volume of component i
WL - Weir length
ω - Critical accentric factor of component i
w - Un-normalized eigenvectors
x - NOC mean
1x - Shifted mean
xi - ith observation in the process
xij - Value of the i-th row and j-th column matrix sijx - Standardized variable
x - Liquid phase mole fraction
xix
xS - Sidedraw mole fraction
xRe - Reflux mole fraction
xP - pumparound liquid mole fraction
xD - Distillate mole fraction
γi - Liquid phase activity coefficient for component i
y - Vapor phase mole fraction
zi - The ith EWMA statistic
Zci - Critical compressibility factor for component i
iφ - Vapor fugacity coefficient for component i
Λij - Wilson binary interaction parameter for component i and j
xx
LIST OF ABBREVIATIONS
APC - Automatic Process Control
DoF - Degree of Freedom
EWMA - Exponential Weight Moving Average
FDD - Fault Detection and Diagnosis
ISPC - Improved Statistical Process Control
MA - Moving Average
MESH - Mass, Equilibrium, Summation, Heat
MR - Moving Range
MSA - Multivariate Statistical Analysis
MSPC - Multivariate Statistical Process Control
NIPALS - Non-iterative Partial Least Squares
NOC - Normal Operating Condition
OC - Out of Control
PCA - Principal Component Analysis
PCorrA - Partial Correlation Analysis
PV - Process Variable
QV - Quality Variable
SPC - Statistical Process Control
USPC - Univariate Statistical Process Control
xxi
LIST OF APPENDICES
APPENDIX TITLE PAGE
A Column profile comparison 155
B Parameter selection to design EWMA chart 158
C Parameter selection to design MAMR chart 163
D Number of fault causes 170
CHAPTER 1
INTRODUCTION
1.1 Introduction
A major technological challenge facing the processing industries is the need
to produce consistently high quality product. This is particularly challenging in high
demanding situations where processes are subject to varying raw material properties,
changing market needs and fluctuating operating conditions due to equipment or
process degradation. The need to provide industry with techniques, which enhance
process performance, will require new methodologies to be adopted that are capable
of being used across a spectrum of industrial processing operations and on a wide
range of products (Simoglou et al., 2000).
Modern industrial processes typically have a large number of operating
variables under closed loop control. These loops used to compensate for many types
of disturbances and to counteract the effect of set point change. This is necessary to
achieve high product quality and to meet production standards. Although these
controllers can handle many types of disturbances, there are faults in the process
such as line blockage, line leakage, sensor fault, valve fault and controller fault that
cannot be handled adequately. In order to ensure that process is operating at normal
operating condition as required, faults must be detected, diagnosed and removed.
These activities, and their management, are called as Statistical Process Control, SPC
(Miletic et al., 2004).
2
The combination of Statistical Process Control (SPC) charts and multivariate
analysis approach is used for Fault Detection and Diagnosis (FDD) in the chemical
process. Principal Component Analysis (PCA) and Partial Correlation Analysis
(PCorrA) are the techniques used in this study. A precut multicomponent distillation
column that has been installed with controllers is used as the study unit operation.
Improved Statistical Process Control method is implemented to detect and diagnose
various kinds of faults, which occur in the process.
1.2 Research Background
Statistical methods are used to monitor the performance of the process over
time in order to detect any process shifts from the target. Most of Statistical Process
Control (SPC) techniques involve operations on single response variables such as
weight, pH, temperature, specific gravity, concentration and pressure. This
traditional SPC is used to monitor and verify that the process remains in statistical
control based on small number of variables. The state of statistical control means that
the process or product variables remain close to the target. Normally the fault in the
process is seek through the usage of SPC chart, i.e., the final product quality
variables. Measuring quality variables alone are not enough to describe the process
performance (Kourti et al., 1996). In this study, both quality variables and process
variables are monitored. This can be done by developing the correlation coefficient
between quality variables and process variables using multivariate analysis
technique. In traditional SPC, once the quality variables detected out of statistical
control signal, it is then left up to process operators and engineers to try to diagnose
the cause of out of control using their process knowledge (MacGregor and Kourti,
1995).
Chemical processes are becoming better instrumented with the advances of
process sensors and data acquisition systems. There are massive amount of data
being collected continuously and these variables are often correlated. Multivariate
statistical analysis has been developed in order to extract useful information from
process data and utilize it for process monitoring (Kresta et al., 1991). Normally,
3
multivariate statistical analysis technique is combined with SPC chart using
Hotelling’ s T2 and Q statistics to plot the graph for fault detection and diagnosis.
Even though this conventional method provides good results for fault detection, there
is difficulty in applying this method to diagnose faults because it does not provide a
causal description of the process that can be used as the basis for fault diagnosis.
Currently, contribution plots are used as the basic tools for fault diagnosis in the
multivariate statistical approaches. However, this plot cannot exactly diagnose the
cause but it just provides greater insight into possible causes and thereby narrows the
search. The cause of the faults cannot be found in a straightforward manner.
To overcome the limitation of contribution plot using multivariate analysis
technique to diagnose fault, Improved SPC chart is introduced in this study.
Multivariate analysis approach is applied in the SPC realm procedure to detect and
diagnose the faulty condition in different approach. The multivariate analysis method
is used to develop the control limits of SPC charts. The correlation coefficient
calculated from multivariate analysis technique is applied to improve the SPC chart.
The quality variables data is incorporated in the control chart during the faulty
condition for fault detection purpose, while the process variables which has been
correlated with the quality variables is used for fault diagnosis. Therefore, the
Improve SPC charts applied is not only for quality variables but also for process
variables. By monitoring the process variables, the cause of faulty condition, which
affects the quality variables, could be identified directly. This will help the operator
to take proper action immediately after faults exist in the process.
4
1.3 Objectives of the Research
1. To determine the performance of the Improved Statistical Process Control
charts; which are Shewhart individual and Shewhart range, Exponential
Weight Moving Average (EWMA) and Moving Average and Moving
Range (MAMR) chart for fault detection.
2. To utilize multivariate analysis technique, Principal Component Analysis
(PCA), and Partial Correlation Analysis (PCorrA), for developing the
relationship between the process variable(s) and the quality variable(s) for
fault diagnosis.
1.4 Scopes of the Research
The scopes of the research are:
1. A simulated precut multicomponent distillation column model from
the literature is used as a case study. The model consists of
controllers with various kinds of disturbances and operating
conditions.
2. A set of Normal Operating Condition (NOC) data and a set of Out
of Control (OC) data are generated using this simulated distillation
column.
3. Normal operating statistical model is developed using the
multivariate techniques, PCA and PCorrA via correlation
coefficient approach between the quality variable(s) and the process
variable(s).
4. The Shewhart individual and Shewhart range, Exponential Weight
Moving Average (EWMA), and Moving Average and Moving
Range (MAMR) charts are developed.
5. The faulty condition is incorporated into the process model in order
to see the performance of the control charts to detect the fault(s)
and to find the cause of the fault(s).
5
6. The results of fault detection and diagnosis are then discussed
further.
1.5 Contributions of the Research
In this research, a new approach known as Improved Statistical Process
Control for fault detection and diagnosis is introduced. Multivariate analysis
technique, Principal Component Analysis, PCA and Partial Correlation Analysis,
PCorrA are used to develop the correlation coefficient between quality variables and
process variables. This technique is incorporated in the Improved SPC chart as a
fault diagnosis tools to find the cause of the faulty condition. Improved SPC charts
are applied for both quality variables and process variables which have been
correlated with quality variables of interest.
1.6 Chapter Summary
This thesis contains seven chapters. The first chapter comprises of the
introduction of the research, research background, objectives of the research, scopes
of the research and contributions of this research. Chapter 2 reviews the multivariate
analysis techniques and the concept of multivariate analysis technique used in this
study, which are Principal Component Analysis (PCA) and Partial Correlation
Analysis (PCorrA).
Chapter 3 consists of the concept of Statistical Process Control, SPC chart,
detail explanation on SPC charts; Shewhart, EWMA and MAMR and the way to
construct these charts. This chapter also presents the implementation of multivariate
analysis technique in SPC chart to develop Improve SPC chart.
Chapter 4 expresses the reasons for choosing distillation column as the case
study. This chapter also presents the dynamic modeling of the columns, formulation
6
of dynamic simulating algorithm, establishment of dynamic simulation program,
controller tuning and explanation on Automatic Process Control, APC time
sampling. The performances of the written simulation program are compared with
HYSYS simulator.
Chapter 5 mainly contains the procedure for fault detection and diagnosis.
This chapter contains variables selection to perform process fault detection and
diagnosis, determination of SPC sampling time, generating of normal operating
condition data, out of control data and the development of correlation coefficient
using PCA and PCorrA to relate the quality variables with process variables.
Chapter 6 presents the result and discussion of the research. The results are
systematically presented. Discussions are made on the performance of each
Improved SPC chart to detect known fault in the process and the efficiency of the
proposed method to conduct fault diagnosis with application of multivariate
statistical analysis. Chapter 7 contains the conclusions of the research and
suggestions to the future SPC research activities.
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