Practical process control design with industrial applications / (Record no. 89472)

000 -LEADER
fixed length control field 08373cam a2200421 i 4500
005 - DATE AND TIME OF LATEST TRANSACTION
control field 20250205114050.0
006 - FIXED-LENGTH DATA ELEMENTS--ADDITIONAL MATERIAL CHARACTERISTICS--GENERAL INFORMATION
fixed length control field m o d
007 - PHYSICAL DESCRIPTION FIXED FIELD--GENERAL INFORMATION
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008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 250205b ||||| |||| 00| 0 eng d
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 1394246501
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 139424651X
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 1394246528
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 9781394246502
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 9781394246519
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number 9781394246526
Qualifying information electronic book
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
Cancelled/invalid ISBN 9781394246496
Qualifying information hardcover
035 ## - SYSTEM CONTROL NUMBER
System control number (OCoLC)1427063192
041 ## - LANGUAGE CODE
Language code of text/sound track or separate title eng
042 ## - AUTHENTICATION CODE
Authentication code pcc
050 04 - LIBRARY OF CONGRESS CALL NUMBER
Classification number TS156.8
Item number .K855 2024
082 00 - DEWEY DECIMAL CLASSIFICATION NUMBER
Classification number 660/.2815
Edition number 23/eng/20240315
100 1# - MAIN ENTRY--PERSONAL NAME
Preferred name for the person Kugelman, Alan M.,
Authority record control number https://id.loc.gov/authorities/names/no2024028489
Relator term author.
245 10 - TITLE STATEMENT
Title Practical process control design with industrial applications /
Statement of responsibility, etc Alan M. Kugelman.
264 #1 - PUBLICATION, DISTRIBUTION, ETC. (IMPRINT)
Place of publication, distribution, etc Hoboken, New Jersey :
Name of publisher, distributor, etc Wiley,
Date of publication, distribution, etc [2024]
300 ## - PHYSICAL DESCRIPTION
Extent 1 online resource (xv, 622 pages) :
Other physical details illustrations (some color)
336 ## - CONTENT TYPE
Content type term text
Content type code txt
Source rdacontent.
337 ## - MEDIA TYPE
Media type term computer
Media type code c
Source rdamedia.
338 ## - CARRIER TYPE
Carrier type term online resource
Carrier type code cr
Source rdacarrier.
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc Includes bibliographical references and index.
505 0# - CONTENTS
Formatted contents note Table of Contents<br/>Preface xiii<br/><br/>1 Process Dynamics and Process Control Overview 1<br/><br/>1.1 Introduction 2<br/><br/>1.2 The Role of Process Control 3<br/><br/>1.3 Tag Naming Conventions 4<br/><br/>1.4 Control Loop Essentials 7<br/><br/>1.5 Process Dynamics and Dynamic Responses 14<br/><br/>1.6 Plant Testing 25<br/><br/>1.7 Classification of Process Control Strategies 28<br/><br/>1.8 Benefits of Control Applications 41<br/><br/>2 Feedback Control Essentials 44<br/><br/>2.1 Introduction 45<br/><br/>2.2 Single Loop Control, Simple, and Complex Cascades 46<br/><br/>2.3 Digital Control System (DCS)Work Environment 50<br/><br/>2.4 PID Control Algorithm Basics 57<br/><br/>2.5 Noise, Filters, Plant Testing, and Closed-Loop Control 93<br/><br/>2.6 Ratio Control 97<br/><br/>2.7 Single Input-Single Output Model-Based Control (MBC) 104<br/><br/>2.8 Cascade Wind-up 112<br/><br/>3 Feedforward Control Essentials 120<br/><br/>3.1 The Role of Feedforward Control 120<br/><br/>3.2 Ratio Control and Steady-State Feedforward Control 124<br/><br/>3.3 Dynamic Compensation via the Lead-Lag Algorithm 126<br/><br/>3.4 Ratio Control and Dynamic Feedforward Control 130<br/><br/>3.5 Incremental Steady-State Feedforward Control 133<br/><br/>3.6 Incremental Dynamic Feedforward Control 137<br/><br/>3.7 Engineering Relationships That Provide Feedforward Corrections 141<br/><br/>4 Process Analysis and Understanding 155<br/><br/>4.1 Business Drivers, Operating Plans, and Operational Objectives 156<br/><br/>4.2 Obtaining Useful Information 156<br/><br/>4.3 Use of Process Analysis 158<br/><br/>5 Split Range Control 178<br/><br/>5.1 Split Range Control Overview 178<br/><br/>5.2 Split Range Control Applications 181<br/><br/>6 Override Control 195<br/><br/>6.1 Override Control Overview 195<br/><br/>6.2 Override Control Applications 198<br/><br/>6.3 From Override Control to Conventional Constraint Control 205<br/><br/>7 Conventional Constraint Control 208<br/><br/>7.1 DMC’s Role in Multivariable Constraint Control 209<br/><br/>7.2 Introduction to Conventional Constraint Control 210<br/><br/>7.3 Natural Draft Heater Combustion Control via Conventional Constraint Control 210<br/><br/>7.4 Maximizing Heat Recovery 218<br/><br/>7.5 Conventional Constraint Control Cascade Structure 226<br/><br/>7.6 Alternate Signal Selector Locations in Constraint Control Designs 228<br/><br/>7.7 Active Constraint Variable Switches 231<br/><br/>7.8 Constraint Control Design Issues 233<br/><br/>8 Design Considerations 236<br/><br/>8.1 First Steps: Process Understanding and Operating Objectives 237<br/><br/>8.2 Basic Control Attributes, Control Options 238<br/><br/>8.3 Standard DCS Functionality 243<br/><br/>8.4 Corporate and Site Standards 244<br/><br/>8.5 Sample Time, Control Frequency and Controller Scheduling 246<br/><br/>8.6 Calculated Control Variables 246<br/><br/>8.7 Inferential Variables 247<br/><br/>8.8 Input Validation 252<br/><br/>8.9 Flow Compensation 258<br/><br/>8.10 Cascade Initialization and Wind-up Protection 259<br/><br/>8.11 Alarming and Operator Messaging 260<br/><br/>8.12 Interactions with Other Control Strategies 261<br/><br/>8.13 Testing to Judge Control Strategy Acceptability 263<br/><br/>9 Level Control 265<br/><br/>9.1 Introduction 265<br/><br/>9.2 Single Loop Level Control 266<br/><br/>9.3 Light-ends Tower Inventory Control 268<br/><br/>9.4 Level Controllers that Manipulate Multiple Flows 273<br/><br/>9.5 More Complex Level Control Applications 277<br/><br/>9.6 Averaging and Tight Level Controller Tuning 286<br/><br/>10 Heat Input/Heat Removal Controls 291<br/><br/>10.1 Introduction 291<br/><br/>10.2 Feed Preheat Controls 295<br/><br/>10.3 Control Strategies in Heat Integrated Units 311<br/><br/>10.4 Fired Heater Firing Controls 323<br/><br/>11 Energy Conservation Controls 339<br/><br/>11.1 Heat Recovery Maximization 340<br/><br/>11.2 Lowering Fired Heater Stack Excess O2 Targets 357<br/><br/>11.3 Reducing Tower Reboiler Duty and Reflux Flow 370<br/><br/>11.4 Reducing Stripping Steam Utilization 383<br/><br/>11.6 Reducing Reactor Treat Gas, Recycle Gas Flows 397<br/><br/>12 Tower Product Quality Controls 410<br/><br/>12.1 Tower Basics 412<br/><br/>12.2 Two-product Towers - Process Variable Summary 412<br/><br/>12.3 Two-product Towers - Common Product Quality Control CV-MV Pairs 419<br/><br/>12.4 Towers with Sidestream - Process Variable Summary 427<br/><br/>12.5 Towers with Sidestream - Common Product Quality Control CV-MV Pairs 432<br/><br/>12.6 Cutpoint, Fractionation, and Their Impact on Tower Operations 435<br/><br/>12.7 Two-product Towers - Overview of Conventional Advanced Control Applications 443<br/><br/>12.8 Towers with Sidestream - Overview of Conventional Advanced Control Applications 453<br/><br/>12.9 Two-product Towers - Conventional Advanced Control Application Examples 463<br/><br/>12.10 Towers with Sidestream - Conventional Advanced Control Application Examples 485<br/><br/>13 Fractionator Product Quality Control 497<br/><br/>13.1 Fractionator Unit Characteristics 499<br/><br/>13.2 Feed True Boiling Point (TBP) Distillation Curve, Cutpoint, and Fractionation 505<br/><br/>13.3 Crude Distillation Unit, CDU - The Most Important Primary Fractionator 515<br/><br/>13.4 Reactor Effluent Product Separation Section Main Fractionators 541<br/><br/>14 Reactor Conversion Control 554<br/><br/>14.1 Reactor Control Fundamentals 555<br/><br/>14.2 Reactor System Unit Configurations 564<br/><br/>14.3 Reactor System Control Objectives, CVs, MVs, and DVs 581<br/><br/>14.4 Conventional Reactor Advanced Control Applications 584<br/><br/>Control, Inlet Temperature Maximization 608<br/><br/>References 613<br/><br/>Index 615
520 ## - SUMMARY, ETC.
Summary, etc "Process design is based on steady state conditions -- process variables, and physical and chemical parameters, are assumed known, fixed and time invariant. However, refinery and chemical plant operations are never at steady state, and it is the transient nature of real-world operations that makes process control an essential requirement for achieving safe and acceptable plant performance. The primary roles of the process control strategies implemented in an operating plant are to (i) hold plant operations at a desired operating point despite process upsets, (ii) provide smooth, fast and safe transitions from one operating point to another, and (iii) keep plant operations on the safe side of limiting process constraints. The control strategy design fundamentals described and discussed are applied to develop numerous specific control strategies in a wide variety of realistic process configurations."--
Assigning source Provided by publisher.
545 0# - BIOGRAPHICAL OR HISTORICAL DATA
Biographical or historical note About the Author<br/>Alan M. Kugelman, PhD, has more than 40 years’ experience in process control application design and implementation in capital projects, DCS migration projects and DCS modernization projects. Working for ExxonMobil Research and Engineering Company (Florham Park, NJ, later in Fairfax, Va.), he developed his process control applications design and implementation expertise during three onsite assignments at ExxonMobil sites in Europe and Japan. He then supported ExxonMobil control applications activities, in both refineries and chemical plants worldwide, from central engineering offices in Brussels, Florham Park, and Fairfax. He developed, and taught company-administered control application training courses to site control engineers worldwide.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name as entry element Process control.
Authority record control number https://id.loc.gov/authorities/subjects/sh85107135.
655 #4 - INDEX TERM--GENRE/FORM
Genre/form data or focus term Electronic books.
856 40 - ELECTRONIC LOCATION AND ACCESS
Uniform Resource Identifier https://onlinelibrary.wiley.com/doi/book/10.1002/9781394246526
Link text Full text is available at Wiley Online Library Click here to view
942 ## - ADDED ENTRY ELEMENTS
Source of classification or shelving scheme
Item type EBOOK
Holdings
Withdrawn status Lost status Source of classification or shelving scheme Damaged status Use restrictions Not for loan Permanent Location Current Location Date acquired Source of acquisition Full call number Date last seen Price effective from Item type
        In Process   COLLEGE LIBRARY COLLEGE LIBRARY 2025-02-05 Megatexts Phil. Inc. 660.2815 K954 2024 2025-02-05 2025-02-05 EBOOK