Index. INDEX_p /15/02 3:08 PM Page 765

Similar documents
Index Accumulation, 53 Accuracy: numerical integration, sensor, 383, Adaptive tuning: expert system, 528 gain scheduling, 518, 529, 709,

Twin-Screw Food Extruder: A Multivariable Case Study for a Process Control Course

Feedback Control of Linear SISO systems. Process Dynamics and Control

Guide to Selected Process Examples :ili3g eil;]iil

Introduction to. Process Control. Ahmet Palazoglu. Second Edition. Jose A. Romagnoli. CRC Press. Taylor & Francis Group. Taylor & Francis Group,

Index. Index. More information. in this web service Cambridge University Press

Principles and Practice of Automatic Process Control

Cascade Control of a Continuous Stirred Tank Reactor (CSTR)

Solutions for Tutorial 10 Stability Analysis

Analysis and Synthesis of Single-Input Single-Output Control Systems

University of Science and Technology, Sudan Department of Chemical Engineering.

CM 3310 Process Control, Spring Lecture 21

Subject: Introduction to Process Control. Week 01, Lectures 01 02, Spring Content

1 An Overview and Brief History of Feedback Control 1. 2 Dynamic Models 23. Contents. Preface. xiii

Table of Laplacetransform

Control Introduction. Gustaf Olsson IEA Lund University.

CHBE320 LECTURE XI CONTROLLER DESIGN AND PID CONTOLLER TUNING. Professor Dae Ryook Yang

SRI VENKATESWARA COLLEGE OF ENGINEERING

Process Modelling, Identification, and Control

ChE 6303 Advanced Process Control

Contents. PART I METHODS AND CONCEPTS 2. Transfer Function Approach Frequency Domain Representations... 42

Answers to multiple choice questions

Multi-Input Multi-output (MIMO) Processes CBE495 LECTURE III CONTROL OF MULTI INPUT MULTI OUTPUT PROCESSES. Professor Dae Ryook Yang

Process Modelling, Identification, and Control

CHAPTER 6 CLOSED LOOP STUDIES

CHAPTER 10: STABILITY &TUNING

Enhanced Single-Loop Control Strategies (Advanced Control) Cascade Control Time-Delay Compensation Inferential Control Selective and Override Control

Dr Ian R. Manchester Dr Ian R. Manchester AMME 3500 : Review

Feedback Control of Dynamic Systems

H-Infinity Controller Design for a Continuous Stirred Tank Reactor

Improved Identification and Control of 2-by-2 MIMO System using Relay Feedback

CONTROL SYSTEMS ENGINEERING Sixth Edition International Student Version

Ch 14: Feedback Control systems

Process Control, 3P4 Assignment 6

Process Control & Design

Additional Closed-Loop Frequency Response Material (Second edition, Chapter 14)

Enhanced Single-Loop Control Strategies Chapter 16

Course Summary. The course cannot be summarized in one lecture.

STABILITY OF CLOSED-LOOP CONTOL SYSTEMS

Dynamics and PID control. Process dynamics

CHAPTER 15: FEEDFORWARD CONTROL

Design of Decentralised PI Controller using Model Reference Adaptive Control for Quadruple Tank Process

CONTROL * ~ SYSTEMS ENGINEERING

Pre GATE Pre-GATE 2018

Lecture 5 Classical Control Overview III. Dr. Radhakant Padhi Asst. Professor Dept. of Aerospace Engineering Indian Institute of Science - Bangalore

TS02 - Pre-Instructional Survey

Learn2Control Laboratory

Model Predictive Control Design for Nonlinear Process Control Reactor Case Study: CSTR (Continuous Stirred Tank Reactor)

Lecture plan: Control Systems II, IDSC, 2017

CHEMICAL ENGINEERING

Control of MIMO processes. 1. Introduction. Control of MIMO processes. Control of Multiple-Input, Multiple Output (MIMO) Processes

3.1 Overview 3.2 Process and control-loop interactions

Feedforward Control Feedforward Compensation

Multi-Loop Control. Department of Chemical Engineering,

Analyzing Control Problems and Improving Control Loop Performance

Distributed Parameter Systems

Chapter 8. Feedback Controllers. Figure 8.1 Schematic diagram for a stirred-tank blending system.

Design and analysis of the prototype of boiler for steam pressure control

Advanced control If single-loop feedback control (PID) alone is not good enough

Open Loop Tuning Rules

Digital Control Engineering Analysis and Design

MULTILOOP CONTROL APPLIED TO INTEGRATOR MIMO. PROCESSES. A Preliminary Study

EC CONTROL SYSTEM UNIT I- CONTROL SYSTEM MODELING

Automatic Control Systems

Ali Karimpour Associate Professor Ferdowsi University of Mashhad

ECE317 : Feedback and Control

YTÜ Mechanical Engineering Department

Outline. Classical Control. Lecture 1

A unified double-loop multi-scale control strategy for NMP integrating-unstable systems

Control of Neutralization Process in Continuous Stirred Tank Reactor (CSTR)

Unit 11 - Week 7: Quantitative feedback theory (Part 1/2)

Design of de-coupler for an interacting tanks system

IC6501 CONTROL SYSTEMS

THE DOS AND DON TS OF DISTILLATION COLUMN CONTROL

RELAY AUTOTUNING OF MULTIVARIABLE SYSTEMS: APPLICATION TO AN EXPERIMENTAL PILOT-SCALE DISTILLATION COLUMN

Simulation based Modeling and Implementation of Adaptive Control Technique for Non Linear Process Tank

CHAPTER 3 TUNING METHODS OF CONTROLLER

6.1 Sketch the z-domain root locus and find the critical gain for the following systems K., the closed-loop characteristic equation is K + z 0.

DYNAMIC SIMULATOR-BASED APC DESIGN FOR A NAPHTHA REDISTILLATION COLUMN

MULTILOOP PI CONTROLLER FOR ACHIEVING SIMULTANEOUS TIME AND FREQUENCY DOMAIN SPECIFICATIONS

KINGS COLLEGE OF ENGINEERING DEPARTMENT OF ELECTRONICS AND COMMUNICATION ENGINEERING

Design and Tuning of Fractional-order PID Controllers for Time-delayed Processes

YTÜ Mechanical Engineering Department

Chapter 2. Classical Control System Design. Dutch Institute of Systems and Control

EI6801 Computer Control of Processes Dept. of EIE and ICE

The dos and don ts of distillation column control

Design of Multivariable Neural Controllers Using a Classical Approach

Design and Comparative Analysis of Controller for Non Linear Tank System

Tuning of Internal Model Control Proportional Integral Derivative Controller for Optimized Control

FEEDBACK and CONTROL SYSTEMS

ECE 388 Automatic Control

NonlinearControlofpHSystemforChangeOverTitrationCurve

(b) A unity feedback system is characterized by the transfer function. Design a suitable compensator to meet the following specifications:

Exam in Systems Engineering/Process Control

CBE495 LECTURE IV MODEL PREDICTIVE CONTROL

Control Systems II. ETH, MAVT, IDSC, Lecture 4 17/03/2017. G. Ducard

Subject: BT6008 Process Measurement and Control. The General Control System

Temperature Control of CSTR Using Fuzzy Logic Control and IMC Control

The dos and don ts of distillation column control

An Improved Relay Auto Tuning of PID Controllers for SOPTD Systems

Transcription:

INDEX_p.765-770 11/15/02 3:08 PM Page 765 Index N A Adaptive control, 144 Adiabatic reactors, 465 Algorithm, control, 5 All-pass factorization, 257 All-pass, frequency response, 225 Amplitude, 216 Amplitude ratio, 218, 222 Anaerobic sludge digester, 725 Analog, 15 Anesthesia, 694 Antireset windup, 346 external, 350 Arrhenius rate expression, 46 Art of process engineering, 527 Automatic tuning, 354 Autoregressive models, 136 B Backwards shift operator, 137, 752 Batch reactor, 679 Bias, 157 Biochemical reactors, 631 Biomedical control, 691 Blending system, 383 ratio control, 373 Block diagram, control, 159 Blood glucose control, 694 Blood pressure control, 698 Bode diagrams, 219, 622 Bode stability criterion, 230 Bypass valve, 17 C Cascade control, 314 Case study, 721 Characteristic equation, 164 Characteristic polynomial, 82 Chemical reactor cascade control, 318 ethylene glycol, 39 exothermic, jacketed, 641 isothermal, 39, 605 propylene glycol, 646 Closed-loop oscillation-based tuning, 198 Closed-loop stability, 173 Closed-loop transfer function, 164 multivariable, 435 Closed-loop time constant, 165 Cohen-Coon tuning, 202 Compartmental models, 692 Compressor control, 463 Constitutive equations, 44 Constraints control problem, 3 windup, 346 MPC, 503 Control and instrumentation diagram, 7 Control horizon, 490 Control objectives, 2 Controller output, 160 Controller pairing, 382, 385 Controller parameters derivative time, 172 integral time, 169 proportional gain, 157 proportional band, 173, 736 Control valves, bypass, 17 equal percentage, 741 gain, 159 installed characteristic, 746 linear, 741 quick opening, 741 Conversion, 42 Critical care, 698 Critical gain, 198 Crossover frequency, 622 Current-to-pressure transducer, 737 D Damping factor, 103 Damkohler number, 42 Deadband, 156 autotuning, 357 Decoupling, 453 Demand-side control, 462 Derivative control, 172 Deviation variables, 59, 64 Differential Pressure (DP) cell, 735 Digital control, 749 765

INDEX_p.765-770 11/15/02 3:08 PM Page 766 766 Index Direct synthesis, 203 Distillation control, 704 step response, 134 Disturbance transfer function, 162 rejection, 178 Drug infusion, 727 Dynamic Matrix Control (DMC), 493 E Eigenvalue, 82 Effective gain (one loop closed), 392 Empirical models autoregressive, 136 first-order + dead time, 129 integrator + dead time, 133 Energy balances, 48 Enthalpy, 50 Evironmental issues, 4 Error, 157 Ethylene glycol reactor, 39 Euler integration, 59 Exothermic CSTR, 83 External reset, 350 F Factorization, 256 all-pass, 257 discrete, 756 multivariable, 443 Failure sensitivity, 402 Fail-closed valve, 4, 738 Fail-open valve, 4, 158, 738 Feedback control, 4, 155 Feed-forward control, 4, 324 Final value theorem, 89 calculating offset, 166 discrete, 139 First-order process, 97 stirred tank heater, 99 First-order + dead time (FODT) estimation, 129 frequency response, 223, 235, 618 Flowmeter orifice plate, 735, 739 Fluidized catalytic cracking (FCCU), 725 Frequency response, 215 Function files, 554 Fundamental models general form, 56 Furnace control, 314 air-fuel ratio, 374 with heat exchanger, 466 G Gain controller, 157 process, 97 valve, 159 Gain margin, 231, 622 Gain scheduling, 359 Gas surge drum, 37 Generalized predictive control (GPC), 507 H Heat capacity, 50 Heat exchanger control, 464 Heat transfer, 47 HDA (hydrodealkylation), 473 Hysteresis, 649 autotuning, 357 I IDCOM, 507 Ideal gas law, 45 Initial value theorem Laplace transforms (continuous), 89 Z-transforms (discrete), 139 Instrumentation, 15 Integral control, 169 Integral time, 169 Integral windup, 346 Integrating process gas surge drum, 37 impulse response, 101 steam drum, 661 step response, 81, 101 surge vessel, 18, 669 transfer function, 168 Integrator + dead time, 133 Internal instability, 207, 254 Internal model control (IMC), 245 block diagram, 263 design for disturbances, 273 design procedure, 265 digital, 756 filter, 266 multivariable, 440 IMC-based PID, 285

INDEX_p.765-770 11/15/02 3:08 PM Page 767 Index 767 disturbance rejection, 292 integrating systems, 293 stable systems, 289 time-delay systems, 294 unstable systems, 301 Input constraints, 275, 346 disturbance, 2, 57 manipulated, 57 Insulin, 694 Interaction, 381 Inverse response, 109, 112 isothermal reactor, 605 steam drum, 661 J Jacketed tank heater, 65, 376 Jacketed batch reactor, 679 Jacketed CSTR, 641 L Laplace transforms definition, 85 derivative, 86 exponential, 85 impulse, 88 pulse, 87 step, 87 time-delay, 86 Lead-lag transfer function, 110 Level control steam drum, 258, 266, 661 surge vessel, 5, 156, 669 Linearization, 60 LTI models, 585 Lumped parameter system, 32 M MATLAB tutorial, 539 frequently used functions, 556 Master controller, 315 Material balances, 36 Matrix notation, 541 m-files, 552 Mean value theorem differential calculus, 35 integral calculus, 35 Model length, 491 Model Predictive Control (MPC), 487 Modeling, 31 Models definition, 17 empirical, 127 fundamental, 31 Modules MATLAB, 539 SIMULINK, 559 ODE, 573 LTI, 585 isothermal CSTR, 605 FODT, 619 biochemical reactor, 631 CSTR, 641 steam drum level, 661 surge vessel level, 669 batch reactor, 679 biomedical, 691 distillation, 703 case study, 721 flow, 733 digital, 749 Monod kinetics, 632 Multiple input multiple output, 382 Multiple steady states biochemical reactor, 633 exothermic CSTR, 648 van de Vusse reactor, 606 N Nonlinear PID, 359 surge vessel, 672 Nonminimum phase, 225 Numerator dynamics, 107 Numerical integration, 58, 573 Nyquist plots, 221, 622 Nyquist stability criterion, 231 O Objective, control, 2 Offset, P-control, 165 Objective function, 490 On-off control, 156 Open-loop control, 247 Operability, 428 Optimization plantwide, 466 MPC, 488 Ordinary differential equations general form, 57

INDEX_p.765-770 11/15/02 3:08 PM Page 768 768 Index numerical solution, 59, 574 ode45, 574 Orifice plate flowmeter, 735, 739 Output variables, 3, 18 measured, 3 unmeasured, 3 Overshoot, 107 Override control, 373 P Packed bed reactor, 374 Padé approximation, 114 Pairing, controller, 382, 385 Parameters, 57 estimation, 140 Perturbation variables, 81 Petroleum refining, 467 Pharmacokinetics, 692 Phase angle, 218, 222 Phase equilibria, 47 Phase margin, 232, 622 Philosophy of process engineering, 527 Physical realizability, Plantwide control, 453 Pole-zero cancellation, 635 Poles continuous, 111 discrete, 137 Potential energy, 49 Primary controller, 315 Process gain estimation, 129 Process model, 256 Proper transfer function, 249 semiproper, 249 strictly proper, 249 Proportional band, 173, 736 Proportional control, 157 Proportional gain, 157 Proportional-integral (PI) control, 169 Proportional-integral-derivative (PID), 172 discrete, 751 Propylene glycol reactor, 646 Pump head curve, 743 Purge stream, 474 Q Quadratic formula, 83 Quadratic programming, 501 Quadruple tank, 423 R Ratio control, 372 Reactive ion etching, 723 Recirculating heat transfer system, 652 Recycle systems, 455 dynamic effects, 459 steady-state effects, 455 Relative gain array (RGA), 392 Relative order, 107, 227, 750 Relative volatility, 47 Relay autotuning, 354 Reset windup, 346 antireset windup (ARW), 346 external ARW, 353 Residence time, 42 Right-half-plane transmission zeros, 421 zeros, 109 Rise time, 108 Robustness, 216, 235 Root locus, 177 Roots, polynomial, 83 Rotary lime kiln, 724 Routh array, 173 Routh stability criterion, 173 S Safety, 4 Sample time, 497, 755 Saturation, 346 Scale-up, 53, 632, 647 Scaling, 424 Second order process, 103 step response, 104 Secondary controller, 315 Selective control, 373 Self-regulating process, 38 Sensitivity, 399 directional, 428 failure, 400 model error, 402 Setpoint, 5 Shower control analysis, 12 SIMULINK tutorial, 559 block diagram, 564 PID controller, 564 Simulation control system, 563

INDEX_p.765-770 11/15/02 3:08 PM Page 769 Index 769 Singular value decomposition (SVD), 429 distillation, 712 Slave controller, 315 Snowball effect, 455 Split-range control, 374 batch reactor, 680 CSTR, 656 Stability, 82 discrete, 138 discrete closed-loop, 753 necessary condition, 174 sufficient condition, 174 State space models, 64, 81 State variables, 18, 57 Steady-state, 58 Steam drum level, 661 feedback control, 663 feedforward control, 661 three-mode control, 666 Step response continuous, 31 discrete, 144, 599 first-order process, 98 MATLAB, 119, 599 second-order process, 104 Stirred tank heater, 50, 99 jacketed, 65, 376 mixer, 425, 433 isothermal reactor, 39 Substrate inhibition kinetics, 632 Supply-side control, 462 Surge vessel control objectives, 5 gas, 37 model, 18 nonlinear control, 669 step response, 102 T Time constant estimation, 129, 132 Time-delay, 86, 113 estimation, 132 Textbooks, control, 20 Thermodynamics, 49 Transducer current-to-pressure (I/P), 737 pressure-to-current (P/I), 737 Transfer functions, closed-loop, 164 first-order, 97 general form, 96 matrix, 386, 421 second-order, 103 Transmission zeros, 421, 444 Transpose, matrix, 541 Tyreus-Luyben tuning, 198, 626 U Ultimate gain, 198 Ultimate period, 198 Underdamped, 81, 106 Unit circle, 137, 750 Unstable processes P, PI control, 180 IMC-based PID, 301 V Valve characteristics, 48, 741 Valve gain, 48, 159 van de Vusse reaction, 606 discrete state space, 598 discrete transfer function, 596 frequency response, 232 IMC, 615 input multiplicity, 608 MPC, 501 ODEs, 575 SIMULINK, 567 state space, 586 step response, 93 transfer function, 587 zero-pole-gain, 589 Ziegler-Nichols, 613 van der Waal s gas law, 45 Velocity form, discrete PID, 751 Z Z-transforms, 137, 752 Zero-order hold, 751 Zeros, 111 discrete, 137 right-half-plane (RHP), 112 transmission, matrix, 421 Ziegler-Nichols tuning, 198 closed-loop method, 198 open-loop method, 201

INDEX_p.765-770 11/15/02 3:08 PM Page 770