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7/30/2019 Mass Flow Measurements of Liquids _1082ch1_1
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1
Overall Plant Design
1
1.1
AUDITING EXISTING PLANTS FOR UPGRADING 5
Prerequisites to Auditing 5
Goals 5
Functionality 6
Plant Standards 6
Identify Key Areas for Special Attention 7Who Audits the Plant? 7
The Audit 8
Upgrading Existing Systems 9
Evolution 9
Audit the Installation and Process 10
Process Information and System Integration 11
System Diagnostics and Redundancy 12
References 13
Bibliography 13
1.2
PROJECT MANAGEMENT AND DOCUMENTATION 14
Good Documentation Practices 14
Project Criteria Document 15
The Preferred Vendors/Technology List 15
I&C Documentation System 15
DocumentsPurpose, Contents, and Standard
Formats 18
Process/Mechanical Flow Diagrams 18
Piping and Instrumentation Diagrams 18
The Instrument Schedule 18
Instrument Data Sheets (Specification
Forms) 18System Architecture/Network Diagram 19
Control System Documentation 19
Instrument and Junction Box Layout
Drawings 20
Cable Block Diagrams 20
Control Room Layout Drawings 20
Panel Layouts and General Arrangement 20
Interconnection or Wiring Diagrams 20
Cable Routing, Cableway Sections, and
Details 20
Grounding System Drawings 20
Instrument Loop Diagrams 21
Logic Diagrams 21
Instrument Installation Checkout and
Calibration/Configuration Procedure 21
Decommissioning Documents 21
DocumentationAn Information Management
Perspective 21
Commercial Instrumentation Documentation
Tools 23Project ManagementAn I&C Perspective 23
Project Integration Management 25
Project Scope Management 25
Time Management 26
Cost Management 26
Quality Management 26
Human Resources Management 26
Project Communications 27
Risk Management 27
Procurement 27
Conclusions 27
References 27Bibliography 28
2002 by Bla G. Liptk
http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/http://1082ch1_2.pdf/7/30/2019 Mass Flow Measurements of Liquids _1082ch1_1
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2 Overall Plant Design
1.3
OPERATOR TRAINING, COMMISSIONING,
AND START-UP 29
Commissioning 29
Clear Goals and Objectives 29
Staffing 29
Schedule 32
Communications 32
Pre-Start-Up Inspection 32
Partial Operation and Water Runs 33
Documentation 35
Operator Training 35
Operating Procedures 35
Approach to Training 38
Simulation 38
On-the-Job Training 39
Start-Up 40
Field Changes 40Turnover 40
Post-Start-Up 40
Conclusions 41
Bibliography 41
1.4
FLOWSHEET SYMBOLS AND FUNCTIONAL
DIAGRAMMING FOR DIGITALLY IMPLEMENTED
LOOPS 42
Scope 42
General 42
Application to Industries 42Application to Work Activities 43
Application to Classes of Instrumentation and to
Instrument Functions 43
Extent of Loop and Functional Identification 43
Extent of Symbolization 43
Inclusion of the New S5.1 Standard (now
ANSI/ISA-5.01.01) in User/Owner
Documents 43
Definitions Related to Flowsheet Diagram
Symbology 44
General 44
Definitions 44Identification System Guidelines 47
General 47
Instrument Index 48
Guideline Modifications 48
Multipoint, Multifunction, and Multivariable
Devices 48
Systems Identification 48
Loop Identification Number 49
Typical Instrument Identification/Tag
Number 49
Identification Letter Tables 49
General 50
Graphic Symbol System Guidelines 51
General 51
Guideline Modifications 51
Instrument Line Symbols 51
Measurement and Control Devices and/or
Function Symbols 51
Multipoint, Multifunction, and Multivariable
Devices and Loops 59Fieldbus Devices, Loops, and Networks 61
Comments and Exceptions (Including
Non-ISA Industrial Practice) 61
Fieldbus P&ID Examples: DeviceNet 63
Functional Diagramming for Digital Systems
(ex-SAMA) 63
Instrument and Control Systems Functional
Diagramming 63
Equivalent Loop, Functional Instrument, and
Electrical Diagrams 64
Functional Diagramming Symbol Tables 64
1.5
HISTORICAL DATA STORAGE AND EVALUATION 79
Clarifying the Purpose of the Data System 79
Interactions and Integration with Other
Systems 80
Integration with Maintenance 80
Integration with Management 80
Data Collection 81
Event Data 81
Data Loggers 82
Data Collection Frequencies 82
Architecture of a Data Historian System 83Data Storage 84
Where to Store Data 85
Data Compression 86
Meta-Data 86
The Cost of Data Storage 86
Hardware Selection 87
Backup Media 87
Analysis and Evaluation 88
Data Filtering and Editing 89
System Testing 89
Support of the Data Historian System 89
Security 90Backup, Archive, and Retrieval 90
Bibliography 90
1.6
INTEGRATION OF PROCESS DATA WITH
MAINTENANCE SYSTEMS 91
Plant Floor Systems 91
Maintenance 92
Computerized Maintenance Management
System 92
Condition Monitoring and Predictive
Maintenance 93
Operation and Maintenance Needs 93
2002 by Bla G. Liptk
http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_5.pdf/http://1082ch1_4.pdf/http://1082ch1_3.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_5.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_4.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/http://1082ch1_3.pdf/7/30/2019 Mass Flow Measurements of Liquids _1082ch1_1
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Contents of Chapter 1 3
CMMS Integration 95
Integration Techniques and Business Alliances 96
Summary 97
References 97
1.7
APPLICATIONS, STANDARDS, AND PRODUCTSFOR GROUNDING AND SHIELDING 98
Grounding- and Shielding-Related Standards 98
Power Grounding Basics 99
Grounding, Bonding, and Overload Protection 102
Grounding Electrode Resistance 102
Power Grounding Definitions 102
NEC Article 250 103
Grounding Examples 104
Service Entrance 104
Separately Derived Instrumentation Power
System 105
Single-Point Grounding of Power Supplies 105
The Ungrounded System 106
Resistance Grounding 106
Shielding Theory 106
Lightning 109
Electrostatic Instrument Shielding 110
Differential Amplifiers and Isolators 111
Instrument Power Transformer Shielding 111
Floating vs. Grounded Instruments 111
Isolation Transformers 112
Power Supply Shielding 112
Digital Communications Shielding 112
Magnetic Field Influences 112
EMI and RF Shielding 112
Shielded Cable 113
Intrinsic Safety Grounding and Shielding 113
The Static Electricity Problem 114
Products 114
Conclusion 114
References 115
Bibliography 115
1.8
CONCEPTS OF HIERARCHICAL CONTROL 116Functionality 116
Measurements and Basic Controls (Functional
Section 1) 116
Advanced/Supervisory Controls (Functional
Section 2) 116
Management (Functional Section 3) 117
Hardware Architecture 117
Input/Output Systems 117
Controllers 117
Workstations 118
Communications 118
Architectural Concepts 119Structural Configuration 119
Hardware/Software Interplay 119
Hardware 119
Operating Systems 119
Communication Protocols 120
Application Software 120
System Hierarchy Interplay 121
System Specification, Selection, Design, andImplementation 121
Conclusions 122
Bibliography 122
1.9
ANALOG AND DISCRETE INPUT/OUTPUT, COSTS
AND SIGNAL PROCESSING 123
A/D and D/A Signal Conversions 127
D/A Converters 127
Weighted Current D/A Converter 127
A/D Converters 128
Counter Ramp ADCs 128
Successive Approximation ADC
(Serial) 129
Flash ADCs (Parallel) 129
Data-Acquisition Systems 130
Single-Channel Systems 130
Analog Signal Conditioning 130
Sample-and-Hold Circuits 131
Multichannel Systems 131
Analog Multiplexing 131
Digital Multiplexing 132
Data-Acquisition Boards 132
Digital to Digital I/O 133
Distributed Systems and Networks 133
RS-232-C 133
The GPIB (IEEE 488) 135
VXIbus 136
The Fieldbuses 136
Virtual Instruments 136
Software for Virtual Instrumentation 137
Theory of Signal Acquisition 137
The Sampling Process 137
Quantization 138
Coding 139Unipolar Codes 139
Bipolar Codes 140
Conclusions and Comments 140
Bibliography 140
1.10
ESTIMATING THE COST OF CONTROL SYSTEM
PACKAGES 142
Suppliers 142
Desired Accuracy of the Estimate 142
Clarify Scope and Objectives of This Control
System 143Estimating Techniques 143
2002 by Bla G. Liptk
http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_9.pdf/http://1082ch1_8.pdf/http://1082ch1_7.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_10.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_9.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_8.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_7.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/http://1082ch1_6.pdf/7/30/2019 Mass Flow Measurements of Liquids _1082ch1_1
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4 Overall Plant Design
Software Tools 144
Controller Costs 144
Operator Station Costs 145
Instrumentation 145
Control Valves 145
Motors and Drives 146
Software Costs 146Maintenance Costs 148
Engineering Costs 148
Training and Start-Up Costs 148
Installation Costs 149
Control Room Incidental Costs 149
Taxes 149
Working with Vendors 149
Contingency Costs 149
Estimating vs. Bidding 150Submitting the Budget 150
Bibliography 150
2002 by Bla G. Liptk
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5
1.1 Auditing Existing Plants for Upgrading
G. K. TOTHEROW
Manufacturing is only one part of a business. The needs of the
business can change rapidly from forces outside manufacturing
and the control and information systems must follow and sup-
port the short-term and long-term business goals and needs of
the business. The process of auditing and upgrading control
systems is primarily one of determining engineering solutions
for business problems. Many companies embrace the concept
of continual improvement. These companies constantly review
and evolve plant systems to support their continued improve-
ment in manufacturing.1However, most companies only review
their automation systems in connection with a major project.
There is a good reason for this behavior. It is expensive and
disruptive to the plant operation to upgrade control systems.
Some people recommend auditing existing plant sys-
tems compared with world-class or best-practices stan-
dards. These audits have their place, but the value realized
by upgrading existing systems is in achieving business
needs and goals. The time to stop upgrading plant automa-
tion and information systems is when it is not a good finan-
cial decision as a way to meet the business needs. The only
way to determine if the upgrade to the existing systems is
a good financial decision is to audit the existing systems
against the functionality needed to achieve company and
plant goals. The purpose of this chapter is to provide a
methodology to audit a plant for upgrading systems. A side
benefit to the methodology given is that the justification for
the upgrade project is written from the audit information.
There are two types of plant upgrades. First, there is
what could be described as the maintenance audit to avoid
obsolete components, eliminate worn-out components, or
conform to new regulatory requirements to keep the plant
operating. Then, there is the upgrade for process improve-
ment or manufacturing cost savings that will show a return-
on-investment from the upgrade. Both share the common
theme of keeping the plant achieving business goals. The
goals and the project funding are different but the prerequisites
to the audit, the methodology of the audit, the integration
of old and new components, and the recommendation report
are the same when reviewing a plant system for upgrade.
There are five prerequisites to a meaningful consistent
automation system audit:
1. Understand the company and plant goals.
2. Determine the functionality that is needed from plant-systems to achieve or contribute to those goals.
3. Establish or communicate the plant standard compo-
nents and systems that can be maintained effectively
with the available support personnel and spare parts.
4. Identify key processes, machinery, or areas of the plant
for special attention.
5. Choose the best person to perform the audit.
This section first discusses the five prerequisites to the audits,the methodology for conducting the audits, and particular
issues of integrating new technology into existing plants.
PREREQUISITES TO AUDITING
Every plant and every industry has different equipment, raw
materials, and personnel. It stands to reason that every plant
and industry will have a different recipe to optimize profits.
State-of-the-art controls that reduce variation will not provide
the same return on the investment in one process, one line,
one plant, or one company, as they will in another. The sameis true with respect to head count reduction, reducing main-
tenance costs, and increasing reliability. All these factors are
very important to every manufacturer, but the degree to which
they are important varies between plants, industries, company
financial standing, and the general economy. For this reason
it is of foremost importance to fully understand plant and
company goals and audit systems against those goals.
Plant personnel, corporate experts, or outside consultants
may conduct system audits and make recommendations. The
degree to which they understand the plant will certainly be
different so the purpose of the five prerequisites to an audit is
to ensure that pertinent background information and goals of
the audit are clearly understood. Specific prerequisites to an
audit will need to be contracted or expanded based on the
industry and the scope of the project. The prerequisites here will
give the outside expert a good idea of how to meet the needs
of the company and will help the plant technical person con-
vince others to share the direction and success of the upgrade.
Goals
If this entire section were devoted to the importance of under-
standing company and plant goals, it would still not be enough.
The importance of focusing on project goals and the comple-menting company goals and initiatives cannot be overstated.
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6 Overall Plant Design
Manufacturing is only one facet of a business, and it seldom
drives the company; it swings to the demands of marketing,
sales, design, and other business factors. Manufacturing may
be asked to produce greater quantities, increase quality,
decrease delivery, shave costs, reduce downtime, add grades,
change packaging, or any number of other things to meet
business demands. Understanding the current business goalsis highly important prior to modifying manufacturing systems.
There was a time when only the highest-level people in
the company knew the corporate goals. And under them only
a few people knew the business and manufacturing goals of
the plants. And lower still only a few clearly understood the
department goals. Today, most companies have a mission
statement and a policy of passing down written goals so that
those below can establish supporting goals. Whether easy or
difficult to attain, the company, plant, and area goals are
important to auditing an existing plant because these goals
and company initiatives will be the basis for justifying the
audit recommendations.It is good to be given company, plant, and specific goal
information, but it must be understood that many business
decisions and business information will only be disclosed on
a need to know basis. It is also a fact of some businesses
that goals change rapidly and they may not be communicated
effectively. So, the first work that we do is to write a specific
goal for the audit in terms of the company or plant goal to
communicate effectively the basis for the audit. The audit of
an existing plant for upgrading should always have a specific,
stated goal. The following are some likely goals for the audit:
Reduce variation of product Increase throughput
Increase reliability
Avoid obsolescence
Adhere to safety or environmental regulations
Reduce maintenance costs
Decrease manufacturing changeover or process mod-
ification time
Functionality
The world of plant and process automation is changing very
rapidly. Whereas 25 years ago an operator interface devicemight be a panel with a gauge and push buttons, today the
operator interface device might be a wireless hand-held com-
puter. It is far too easy and common to jump from the project
goal or problem statement to looking for equipment or sys-
tems that a vendor says will solve the problem. An important
intermediate step is to obtain a laypersons description writ-
ten in simple language that tells what the ideal systems
must do for the operators, maintenance mechanics, and man-
agers to allow them to accomplish the stated goal or solve
the problem. Most of the functional description should come
from the users and area process managers along with an
estimate of the financial payback for solving the problem orachieving the goal. The functional description and the esti-
mated return on that functionality are often acquired by inter-
viewing the appropriate operating and maintenance personnel.
One purpose of the written functionality description is that
it breaks the components of the existing plant into digestible
pieces and describes the ideal as established from the goals.
It does so in terms of the functionality rather than component
descriptions. This is necessary because the physical componentoften provides several functionalities. A control system may
provide the controls, operator interface device, alarming, and
other functionality. The system may perform near the level of
the ideal functionality in one or two areas and may perform
far below the ideal functionality in others. The audit recom-
mendations could advocate replacement of the system or it
might recommend add-on components to enhance the system
capability in the poorly performing functional areas.
A second reason for the ideal functionality and the
estimated financial payback for the functionality is that it will
provide an estimate for the preliminary return on investment
for the upgrade project. Better yet, the return for providingthe functionality comes from the plant personnel who must
support the project.
The functional description should address:
Process measurement
Final control element
Input/output system wiring
Control needs
Redundancy
Operator interface needs
Alarm handling needs
Historical process data needs Management information needs
Production/cost/scheduling needs
Maintenance needs
Customer information needs
Plant Standards
Manufacturing and process facilities should establish and main-
tain a list of preferred components and vendors that have the
functionality needed to achieve plant and project goals. Plant
standards are useful to set a general direction in the components
and ways a facility will try to meet company and plant goalsand avoid obsolete components. Other common uses of a stan-
dard is to establish better vendor relationships, minimize spare
parts, minimize decision making, minimize training costs, and
ensure consistent and predictable results. That standards help
in all the ways listed above needs no explanation; however,
using standards to establish general direction and the period of
review of standards needs further clarification.
Few plants can justify the capital financing or the pro-
duction downtime to replace components across the facility
when new devices are proved better to meet the needed func-
tionality or when new industry trends and standards are estab-
lished. Innovation must be integrated into the facility. Theplant standard should lead in setting the direction to keep the
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1.1 Auditing Existing Plants for Upgrading 7
components from becoming obsolete and promoting devices
that will better satisfy the functionality desired. When should
the existing standards be reviewed and modified? The answer
is more often than is done for most plants. Any of the fol-
lowing events signal a time to review plant standards:
The manufacturer announces a discontinuation of theproduct.
An organizational or industry standards committee
selects another standard.
The plant is planning a major expansion or revision.
A problem of service develops with established ven-
dors or manufacturers.
Consider the example below, which shows a company that sets
and changes its plant standards to establish a strategic direction.
A chemical plant built in 1961 installed Foxboro transmit-
ters using 1050 mA DC current signals. Once installed, the
transmitters and wiring worked well and met the functionalitycriteria for field instrumentation and field wiring. Some time
after the ISA standards committee adopted 420 mA DC as
the standard for field signal wiring (ISA S50.1-1972) the plant
decided to adopt the 420 mA transmitters as their new stan-
dard. The next major opportunity to install transmitters was
during a major expansion and renovation project in 1975. The
plant replaced 100 of the old transmitters in the area of the
renovation and put them in the storeroom for spares for the
rest of the plant that kept the old 1050 mA DC transmitters.
In 1999, the plant had another major renovation project.
This time the project convinced the plant to use Foundation
Fieldbus for the signal wiring. The plant adopted FoundationFieldbus as its new standard field wiring. By 2000, 30% of the
plant was using new smart transmitters and Foundation Field-
bus, 65% of the plant was using transmitters with 420 mA DC
signal wiring, and 5% of the transmitters were the old 1050
mA DC Foxboro transmitters. The company will continue to
install the Foundation Fieldbus standard with each project.
The hypothetical plant used the plant standard to set an
appropriate direction to avoid obsolescence and integrated the
new standard along with the old where both met the required
functionality. The 420 mA DC only transmitters and signal
cable will not meet necessary functionality requirements when
the plant demands smart transmitters with online diagnostics.
A final word concerning standards is to guard against
using the standard to thwart innovation that meets the func-
tionality of its intended use and achieves company or project
goals better, faster, or cheaper.
Identify Key Areas for Special Attention
There are key areas, processes, and control loops in every
plant that are crucial to quality, production, or profitability.
They will be referred to as key success areas. These key
success areas and their impact on the operation should be
noted and understood by the auditors prior to reviewing thesystems for upgrading.
The purpose of this prerequisite item is to ensure that
audit recommendations address any issues that might affect
the process or operations at these points. These key areas
may be ISO (International Standards Organization) tagged
control loops, OSHA (Occupational Safety and Health
Administration) regulated areas, FDA (Food and Drug
Administration) certified processes, or just important areasof the plant. The audit to upgrade existing systems in the
plant should specifically address the potential impact to these
regulated areas. The importance of the key success areas of
the plant will be well understood by the operations and man-
agement people that will be curious about how any changes
may affect their operations. There may be some merit in
specifically addressing these areas in the upgrade recommen-
dations even to note that there is no effect on the process or
operation at that point.
The important point to remember is that the information
about these key success areas of plant operation should be
communicated to those responsible for the audit. It is certainthat if the potential impact on these areas is not addressed
up-front, the issue will be questioned later.
Who Audits the Plant?
The last prerequisite before performing the audit is to deter-
mine who should perform the audit. There are several persons
or groups that can be made responsible for the auditing so
the recommendations of this section may be a little difficult
to understand as we have not yet defined all of the steps and
expectations of the audit. This subsection should be reread
after the audit steps are reviewed if the reader disagrees withthe authors opinion.
Websters New World Dictionary2defines audit as follows:
5.any thorough examination and evaluation of a
problem.
The person, or group, conducting the plant review and
making upgrade recommendations should have the time to
dedicate to doing a thorough examination of the existing
systems, experience in evaluating and making appropriate
recommendations to resolve problems, and ability to write a
report that will show the value of implementing the recom-
mendations. Choosing the best person to perform the jobamong the several who regularly perform such tasks is as
important as successful accomplishment of the goals.
Figure 1.1a is a subjective chart showing a rating of the
qualifications of the persons who regularly conduct such
work. The chart shows the ranking of the various people on
a scale of 1 to 5, with 5 the best.
The categories on the chart are explained below.
Plant engineerA technical person at the plant with
3 to 7 years automation experience
Corporate engineerA senior-level engineer who
travels between various plants providing technicaltroubleshooting and project support
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8 Overall Plant Design
VendorA technical salesperson who might be called
to assess the existing systems and make recommen-
dations
Engineering firmAn outside engineer from a firm
that does detail engineering and project management
ConsultantAn individual with extensive technicalbackground and experience who is a specialist in
that process industry or is an expert in the technical
area of the upgrade project
Process knowledgeKnowledge of the plant process
in the area of the audit
Plant knowledgeUnderstanding of the plant, goals,
systems, and personnel
Industry knowledgeUnderstanding of the business,
regulations, projects, and trends for that process
industry
Problem resolutionCapability of determining equip-
ment and system changes that will resolve the tech-nical problems and add the functionality that the
audit reveals
TimeThe dedicated time to study the problem, deter-
mine resolution, and write reports
ExperienceGeneric estimate of the experience each
has in this type of audit and problem resolution
InfluenceAssessment of the capabilities of the per-
son or group to have the recommendations imple-
mented at the plant
CostThe cost of the audit
Project costThe degree to which the auditor will work
without bias on the companys behalf to gain return-on-investment and save capital money on the project
Four of the audit prerequisites are listed to give the out-
side experts the detail plant knowledge that they need to do
a very thorough audit. Unfortunately, there is no efficient
way to transfer the knowledge and experience of the outside
expert to plant personnel. Even if the plant had a technical
person with the time and experience to adequately examineand evaluate systems for upgrading, that plant person may
not have the political influence to be the catalyst for change
that is needed to convince the plant to implement the recom-
mendations.
THE AUDIT
The introduction to this chapter mentioned that there are two
types of projects: the maintenance upgrades to avoid obsolete
components, eliminate problem components, or conform to
new regulatory requirements to keep the plant operating; andthe capital project for process improvement or manufacturing
cost savings that will show a return on investment from the
upgrade. The primary differences between these types of
audits are perhaps the scale of the job and the internal funding
differences. Otherwise, both audits are essentially the same
and share the same characteristics and steps. Either type of
project will require finding the best place to replace the
functionality of the old components with new. Both projects
will require the new components to integrate with old com-
ponents. The maintenance project to replace individual com-
ponents relies more on the plant standards that set strategic
directions to ensure the solutions are synchronized with theplant long-term goals.
Plant Engineer Corporate Engineer Vendor Engineering Firm Consultant
Process
Knowledge5 5 3 4 4
Plant
Knowledge5 5 3 4 4
Industry
Knowledge4 5 3 3 5
Problem
Resolution2 3 4 4 5
Time 2 3 2 5 5
Experience 3 4 3 3 5
Influence 2 3 2 5 5
Cost 4 3 5 2 1
ProjectCost
3 4 2 2 5
FIG. 1.1a
Chart showing a subjective ranking of the relative strengths of persons who might perform a plant audit: 5 is best, 1 is worst.
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1.1 Auditing Existing Plants for Upgrading 9
Now, we understand the company, plant, process area,
and upgrade project goals. We interviewed operations and
management personnel and we know the functional specifi-
cations for an ideal system that would allow operations
achieve the project goals. We have estimates from operators,
managers, and maintenance personnel of the time, product,rework, quality, and other tangible savings that they can
achieve with functionality discussed. We understand the plant
standards for various components in the audited systems. We
identified the key success areas of the plant and noted their
impact on profitability. We selected an auditor and gave him
or her all our background material. So, now what methodol-
ogy should our expert follow?
1. The first step of the audit is to review the prerequisites
with the auditor. Remember that the purpose of the
prerequisites is to share plant-specific knowledge and
establish a functionality that would enable the plantto accomplish the goals.
2. Perform a physical audit of the systems (Figure 1.1b).
Thoroughly examine the existing systems auditing
functionality, models of components, and operating
procedures. Take special notice of communication
ports and communication capability of electronic
devices. Look carefully at the physical condition of
signal wiring and input/output (I/O) systems as well
as the installation of the existing equipment. Note
again that the systems should be audited in functional
groups rather than physical components. The operator
interface device includes at least three functionalgroups: interface to process data and control, alarm
management, and historical data.
3. Define the gap that exists between the functionality
needed and the functionality in the present systems.
Consider submitting this gap analysis for review and
approval by operations and management as an inter-
mediate step.
4. Evaluate the upgrades needed to close or eliminate the
functional gap using plant standard equipment where
applicable.
5. Evaluate the modifications to the operation and main-
tenance practices needed with the system upgrades toachieve and sustain the project goals.
6. Make a formal recommendation of the most effective
upgrade that will evolve the present systems and sup-
ply the functionality needed to achieve the goals of
the project. Recommend the changes needed to oper-
ation and maintenance practices that are necessary to
achieve and sustain improvements. Provide a cost esti-
mate of the upgrade and a rough return on investmentfrom the information gathered in the ideal functional
specification. Define the operating performance goals
that can be achieved by following the recommenda-
tions, and determine the measurable results that will
be the success criteria for the project. The recommen-
dation should also state the estimated length of time
that the system will remain viable.
7. Audit the system performance as compared to the
project goals and the agreed-upon project success cri-
teria approximately 6 months after the upgrade project
is complete.
These seven steps constitute an outline for auditing a
plant for automation system upgrades. The procedure does
not address what to look for or how to evaluate the selection
of various components. Other sections of the Instrument
Engineers Handbook adequately address the selection and
installation of control elements and transmitters, networking,
control systems, operator interface devices, and other tech-
nical information. The last part of this section focuses on a
few of the fundamental issues of the integration of new and
old components in upgrading existing systems.
UPGRADING EXISTING SYSTEMS
The person performing the audit should have knowledge
beyond that of the typical plant personnel of the trends,
alliances, and evolving technologies that will provide a great
return on investment for manufacturing and process industries.
These items may not be in the functional specification. The
auditor has an obligation to make the plant aware of trends,
evolving technologies, and integration issues so that the plant
can determine the value of an immediate investment. The rest
of this section on auditing an existing plant for upgrades
addresses some of the issues of integration of old and newand other items that the auditor should include in the upgrade
recommendation report.
Evolution
Systems should evolve, not become extinct.
Evolution should be the plan while auditing existing sys-
tems and should definitely be a primary consideration in the
evaluation phase of the system upgrade. In the 1980s and
1990s a distributed control system (DCS) meant proprietary
I/O systems, controllers, data highways, operator interface
devices, and process historians from a single vendor. Initialinvestment to purchase these systems was high, and the cost
FIG. 1.1b
List of some of the items that should be noted by observation or
discussions with operators during a control system audit.
Check Sheet for Control System Audits
Model numbers of components
Instrument installation
Communication capability of electronic devices
Physical condition of instruments, valves, controllers, and wiring
Valve position, cycling at typical conditions
Operating procedures, problems, suggestions
Documentation
Problems with regulatory control
Multiple operator interface devices to various systems
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10 Overall Plant Design
of outages and disturbance to operations installing them were
even greater. Suppliers replaced components and had major
new releases often because the systems encompassed both
the hardware and software in many areas of functionality and
because competition and development were very active. A
result is that it is common for customers to have two sys-
tems from the same vendor with new operator interfacedevices that cannot communicate with old controllers, or new
controllers that will not communicate with old operator
devices. Today, many companies operate with independent
systems from various suppliers on the same plant site.
Like others, Fisher Controls, now part of Emerson Process
Management, began assisting customers with life-cycle plan-
ning for the DCS in the early 1990s. These life-cycle programs
provide migration paths to keep systems current and provide
notification of new products and manufacturing changes and
supply of older products.3
(Honeywell offers several options
of LifeCycle Management (LCM) to help its customers inte-
grate new technology with predictable costs.4
) These pro-grams help successfully avoid component obsolescence and
assure that the components interface through several vintages,
but they do not always lessen the cost and disruption to plant
operations. There is another option to supply the evolution
needed.
In the late 1990s open standards, increased functionality,
and reliability of personal computers and the need for process
information combined to enable, and force, vendors to create
access to their systems. Today, a plant system can be defined
as an arrangement of independent components connected to
form a unity for the achievement of specified functionality.
The components do not need to be from one vendor. Archi-tecture of the system is very important. Hardware and phys-
ical connectivity to the proper data highway systems enable
very highly flexible and upgradable functionality through
upgrading software. The components can be selected because
they are the best of breed, or selected on the basis of lowest
cost to fill the functional requirement. With the proper archi-
tecture, the hardware and software components that comprise
the process control and information system can evolve at
different speeds over many years with minimal impact onoperations and minimum cost.
The audit should identify existing components supporting
interfaces to open systems as well as existing components from
suppliers that refuse to provide open interfaces. Figure 1.1c
shows a typical 1990-vintage DCS with a good, high-speed
interface to other systems. Figure 1.1d shows PCs as new
operator interface devices connected with redundant links to
the DCS and PLCs (programmable logic controllers). Addi-
tional functionality is added to the operator interface device
through software to allow retrieval of grade specifications
from the specification management system and downloading
of grade set points and tuning parameters to the existingcontrol systems.
Audit the Installation and Process
Few situations are more frustrating or more futile than trying
to correct process design problems with process control. Sim-
ilarly, changing manufacturers or styles of instruments will
hardly improve the control problems caused by instrument
installation errors. Every control and system upgrade project
should strive to correct the physical process and instrument
installation problem of past projects. Physical problems
involve piping and mechanical work that is usually expensive,and controls engineers are always under pressure to make the
existing system work without modification. However, the best
FIG. 1.1c
Typical DCS architecture circa 1990.
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1.1 Auditing Existing Plants for Upgrading 11
approach is to address the problems directly. Allowing oper-
ations and management to think that a new controller or new
instrumentation will resolve a physical problem is as great a
disservice as failing to recognize the physical problem. Theaudit is the time to recognize and note process and instrument
installation problems.
Sometimes it is not feasible to conduct an audit to scru-
tinize every process and every instrument and control valve
installation looking for installation problems. The process
design problems are particularly difficult to see without ana-
lyzing Process and Instrument Diagrams (P&ID) and yet with
existing systems this is not something that is typically part
of the control system upgrade project. Scrutiny of the process
and control system designs must be focused on certain areas
prior to the field audit.One way to identify process areas for extra scrutiny is
through recognizing indicators of process problems from
other parts of the audit. Figure 1.1e lists some of the key
indicators that a control problem is more involved than just
needing a new controller or upgraded system.
Process Information and System Integration
Great process control is not enough. Process information is
more valuable than control in many industries today. This is
not totally without reason or justification since the information
is needed for product tracking, product genealogy, offline
statistical analysis, regulatory compliance, and marketing andcustomer relations. Process information increasingly interfaces
to enterprise resource planning (ERP) systems, enterprise
asset management (EAM) systems, manufacturing execution
systems (MES), and data historians. Every system audit andrecommendation should address these issues.
The functional specification in the prerequisites to the
audit should contain a statement about the desired interfaces
to other systems. Today, any audit should address this issue
whether it is in the functional specification or not. The trend
is clear that more process information and process system
health information are desired by higher-level systems. It is
also true that the process control system and the operator, or
process manager as the position is often called, increasingly
need access to many more systems than just a process con-
troller. The integration between the management systems will
be bidirectional where quality control persons may need tosee the key information about the current product and the
FIG. 1.1d
Illustration of the same DCS as Figure 1.1c with a new DCS controller, PLC, new operator interfaces, and supervisory controls added.
FIG. 1.1e
Do not try to correct problems and disturbances introduced by poor
process design and nonfunctional process equipment when the best
solution is to recognize and correct the process.
Indications of Physical Process Problems
Control of process was always poor.
Periodic or seasonal fluctuations in controllability of the process.
Instruments and valves that work in other places are not working. Fast oscillations in process characteristic properties after mixing.
Fast process transients and oscillations while in manual mode.
Control valves that operate at extremes of their range.
Excessive process equipment and control component failures.
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12 Overall Plant Design
operator may need to see, approve, and download the spec-
ification for the next run in the plant. Operators, or their
systems, need access to the maintenance system, e-mail,
upstream and downstream processes information, historical
data, time and attendance systems, possibly accounting to
show real-time cost of production, and various other systems
in the future. Figure 1.1f shows the connectivity for the
operator interface devices to integrate to the other plant infor-
mation systems.
System Diagnostics and Redundancy
System diagnostics and redundancy, like process informationand system integration, is an area that the auditor may under-
stand better than the plant personnel. So too, the auditor
making recommendations for upgrading systems should
include recommendations on the system diagnostics and
redundancy even when the functional specification does not
address the issues.
System diagnostics begins with the transmitters and final
control elements in the field. Smart transmitters, valves, and
a device network are the basis for a system to alert folks of
process and instrument problems and provide the diagnostics
to isolate the problem.
The 420 mA DC has been the standard for signal wiringsince the 1960s but it now looks extravagant to run a pair of
copper wires in a plant to every instrument for just one piece of
information. Fieldbus technologies are discussed in Section 4.7.
The plant may need direction and recommendations on the
diagnostic and quality information available.
Regulatory control is as important as ever, but supervi-
sory controls and coordinating plant controls are needed in
most plants to make a step change in quality and productivity.
Changing one regulatory controller for another is not a recipe
for success. Section 1.8 of this chapter discusses hierarchical
control. The auditor must consider that recommendations
address virtual sensors, automatic loop tuning, statistical pro-
cess control, and model-based control. Also, the control sys-
tems recommendations should make the plant aware of
redundancy options, diagnostic capabilities, and automatic
telephone dialing system alarms.
Redundancy of control systems, where it is required, is
often considered a dreaded but necessary expense. Where
applicable, the control system upgrade recommendation
should address the advantages of redundancy for purely eco-
nomic reasons. Systems that continue to function through a
component failure avoid forced downtime, lost product, the
cost of emergency maintenance support, interruptions to pro-
duction scheduling, and other problems. As systems are inte-
grated, redundancy may be needed in communication net-
works, interface devices, and software to ensure that thesystems continue to function through a failure. The technical
FIG. 1.1f
Illustration of the same DCS as in the previous figures with direct operator interface communication to the PLC, and the addition of
interfaces to other plant information systems that need process data.
2002 by Bla G. Liptk
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1.1 Auditing Existing Plants for Upgrading 13
expert must make the plant aware of opportunities. Section 2.9
discusses system architecture for increased reliability.
References
1. Walton, M., The Deming Management Method, New York: Dodd, Mead
& Company, 1986.
2. Websters New World Dictionary, 2nd college ed., New York: World
Publishing Company, 1970.
3. Proceedings 1992 PROVOX Users Group Meeting Report, Austin, TX:
Fisher Controls Company, 1992.
4. Honeywell Web Site, 2001, http://www.iac.honeywell.com/
pulp_paper/Services/InternetServiceLifeCycleMgtContent.htm.
Bibliography
McMillan, G. K., Process Industrial Instruments and Controls Handbook,
5th ed., New York: McGraw-Hill, 1999.
http://1082ch2_9.pdf/http://1082ch2_9.pdf/