PIDControlfor the future



Similar documents
Dr. Yeffry Handoko Putra, S.T., M.T

Best Practices for Controller Tuning

Plant Wide Performance Monitor Bridges Resource Gap

Lambda Tuning the Universal Method for PID Controllers in Process Control

A simple method to determine control valve performance and its impacts on control loop performance

Performance Monitor Improves Performance of FCC At a Refiner in Anacortes, WA

Raffaele Rea GE-Bayer Specialties Srl - Termoli Paolo Belli, Nunzio Bonavita ABB PS&S SpA - Genova ABB - 1 -

stable response to load disturbances, e.g., an exothermic reaction.

FAST METHODS FOR SLOW LOOPS: TUNE YOUR TEMPERATURE CONTROLS IN 15 MINUTES

Advanced Control, Optimization, and Monitoring

PID Tuning Guide. A Best-Practices Approach to Understanding and Tuning PID Controllers. First Edition by Robert C. Rice, PhD

1. s to Z-Domain Transfer Function

Control System Asset Management

+ A B V B NO NC V COM PV PV

EECE 460 : Control System Design

Measurement Products. PID control theory made easy Optimising plant performance with modern process controllers

Practical Process Control For Engineers and Technicians

A Design of a PID Self-Tuning Controller Using LabVIEW

Achieving consistency in multisite installations of PlantTriage.

Stabilizing a Gimbal Platform using Self-Tuning Fuzzy PID Controller

Introduction. Chapter The Motivation

Ziegler-Nichols-Based Intelligent Fuzzy PID Controller Design for Antenna Tracking System

TLK 48 MICROPROCESSOR-BASED DIGITAL ELECTRONIC REGULATOR

Current Loop Tuning Procedure. Servo Drive Current Loop Tuning Procedure (intended for Analog input PWM output servo drives) General Procedure AN-015

Process Control Primer

SAMPLE CHAPTERS UNESCO EOLSS PID CONTROL. Araki M. Kyoto University, Japan

Proceeding of 5th International Mechanical Engineering Forum 2012 June 20th 2012 June 22nd 2012, Prague, Czech Republic

Implementation of Fuzzy and PID Controller to Water Level System using LabView

A Study of Speed Control of PMDC Motor Using Auto-tuning of PID Controller through LabVIEW

The Use of Hybrid Regulator in Design of Control Systems

PID Control. 6.1 Introduction

TwinCAT NC Configuration

Optimized Fuzzy Control by Particle Swarm Optimization Technique for Control of CSTR

PID Controller Tuning: A Short Tutorial

General Specifications

Control of an industrial process using PID control blocks in automation controller

Tadahiro Yasuda. Introduction. Overview of Criterion D200. Feature Article

Loop Scout. Loop and Alarm Performance Management Service

Transient analysis of integrated solar/diesel hybrid power system using MATLAB Simulink

Module Content:

PID Control. Chapter 10

Level Control with DeltaV

SIMULATION AND CONTROL OF BATCH REACTORS

Jump Start: Aspen HYSYS Dynamics V7.3

Power Electronics. Prof. K. Gopakumar. Centre for Electronics Design and Technology. Indian Institute of Science, Bangalore.

Input signal Maximum Range Accuracy. Thermocouple E -50 to 700 C (-58 to 1832 F) ±1 C

Temperature Controller CD401/CD901/CD701/CD501/CD100/CD101 Instruction Manual

Level control with DeltaV

PROCESS CONTROL SYSTEM DESIGN Process Control System Design. LECTURE 6: SIMO and MISO CONTROL

LM118/LM218/LM318 Operational Amplifiers

General Specifications

2Azerbaijan Shahid Madani University. This paper is extracted from the M.Sc. Thesis

Optimization of PID parameters with an improved simplex PSO

Matlab and Simulink. Matlab and Simulink for Control

Enhancing Process Control Education with the Control Station Training Simulator

How To Swap Output Phases Of A Power Supply With A Power Converter

Field Products. Experion LX. Proven, Easy to Use and Purpose-built Distributed Control System

EE 402 RECITATION #13 REPORT

Process Control. Industrial IT solutions for the cement industry

Introduction to SMPS Control Techniques

The Role of Automation Systems in Management of Change

Safe Control of a Pneumatic Muscle Powered System

Artificial Intelligence: Fuzzy Logic Explained

Chapter 10. Control Design: Intuition or Analysis?

Fuzzy Logic Based Reactivity Control in Nuclear Power Plants

A Comparison of PID Controller Tuning Methods for Three Tank Level Process

HONEYWELL DC 1010 / / 1040 DIGITAL CONTROLLER PRODUCT MANUAL /02

Design of Model Reference Self Tuning Mechanism for PID like Fuzzy Controller

Temperature Transmitter TTX300

Available online at Available online at

Control of an Electronic Expansion Valve Using an Adaptive PID Controller

Equalization/Compensation of Transmission Media. Channel (copper or fiber)

PID, LQR and LQR-PID on a Quadcopter Platform

Control Loop Performance Monitoring in a Power Plant

The Japan Society of Mechanical Engineers C 2010

DC1000 Series General Purpose UNIVERSAL DIGITAL CONTROLLERS

A PC-BASED TIME INTERVAL COUNTER WITH 200 PS RESOLUTION

Chilled Water Valves: Resizing and Tuning for Peak Performance. IDEA Conference Feb Jay Russell, PE University of Michigan

CONTROL SYSTEMS, ROBOTICS AND AUTOMATION Vol. XVI - Fault Accomodation Using Model Predictive Methods - Jovan D. Bošković and Raman K.

Temperature Control of Air Heater with DeltaV

ADVANCED CONTROL TECHNIQUE OF CENTRIFUGAL COMPRESSOR FOR COMPLEX GAS COMPRESSION PROCESSES

INPROCESS TRAINING OVERVIEW

DCMS DC MOTOR SYSTEM User Manual

Dynamic Simulation of Induction Motor Drive using Neuro Controller

Improved incremental conductance method for maximum power point tracking using cuk converter

Control System Asset Performance in Oil Refineries

SYL-2342, SYL-2352 PID TEMPERATURE CONTROLLER INSTRUCTION MANUAL Version 4.6 RTD R 4

Keywords: Fuzzy Logic, Control, Refrigeration Systems and Electronic Expansion Valves.

Systems Engineering/Process Control L10

INTERNET BASED DATA LOGGING AND SUPERVISORY CONTROL OF BOILER DRUM LEVEL USING LABVIEW

Delivering NIST Time to Financial Markets Via Common-View GPS Measurements

Process controller Setpoint programmer 1/16 DIN - 48 x 48 mm gammadue series M5 line

Perform Common Process Loop Control Algorithms

Controller Design using the Maple Professional Math Toolbox for LabVIEW

Temperature Control with DeltaV

Transcription:

PIDControlfor the future Haruo TAKATSU Yokogawa Electric Corporation! 1!

Agenda! 2!

Discussion Items 1. Will PID control continue to be used in the future? Market Survey in Japan 2. When and why is derivative action used? Flexibility of PID Control block in DCS 3. What are alternatives? Self-Tuning / Adaptive Control, Internal Model Control 4. What is your favorite tuning method? PID Tuning in our system 5. Do we know everything about PID or are there any research needs? Introduce Monitoring & Diagnosis! 3!

Needs of PID Control SICE Report! 4!

1400 Control Technology Survey 90 Applications 80 1200 70 1000 60 O(Others) PW(Power plant) E(Engineering) CR(Cement and ceramic) 800 Applications 600 50 40 PP(Pulp and paper) CF(Chemical, fiber,film) PC(Petrochemical) R(Refinery) 400 30 20 200 10 0 0 I-PD and 2 degrees of freedom PID PID auto tuning Gain scheduling! 5! Model predictive control Fuzzy control Dead time compensation Decoupling PID Rule based control Optimization Kalman filter Neural network Optimal regulator Observer H infinity control Adaptive control Exact linearizarion Repetitive control Sliding mode control S(Steel and metal) Takatsu, H., Itou, T. : Future Needs for Control Theory in Industry Report of the Control Technology Survey in Japanese Industry, IEEE Transaction on Control Systems Technology, 07, 03 pp.298-305 (1999) Control Technologies

PID Control Structure Derivative Action! 6!

Control Block in DCS! 7!

PID Control DV PID SV - 1 1 T is T d s 100 PB MV Process PV DV PI-D SV - 1 1 T is - Tds α 100 PB MV Process PV DV I-PD 1 T ds 1 αt ds SV 1 - T is 1 Tds - 100 PB MV Process PV! 8! Page 8

PID Alternatives Adaptive / SelfTuning Control! 9!

Self-Tuning Control Estimated Model PID Tuning Model Estimation PID parameters Response Monitoring SV PID Control MV Process PV! 10!

Self-Tuning Control! Nonlinear Programming! Xmid Xmax Xbar Xref Xmin In case oscillating and small overshoot, Xexp Increase/Decrease P and decrease I. Reflection: Xref = (1a)Xbar! axmax In case No oscillation, slow convergence, Expansion: Decrease Xexp= P bxref(1!b)xbar &I. Xmid Xmax Xmid Xred Xmax Xcon Contraction: Xred In case large overshoot and Xcon= fast convergence, cxmax(1!c)xbar Xmin Increase/decrease P & I.! 11! Reduction In case slow oscillation and convergence, Decrease P and increase I.

PID Alternatives IMC Control! 12!

Internal Model Control DV Q(s) SV MV PV C(s) P(s)! - P M (s) P M (s) - DV C(s) SV MV PV Q(s) P(s)! P M (s) - Controller:C(s), Internal Model: P M (s), Process:P(s)! 13!

Internal Model Control SV Kc(1T P s) MV PV 1λT P(s) P s! K P e!lp s 1T P s! 14! 2012.1.6-20

PID Tuning Method IMC Method! 15!

PID Tuning Stable Process Gain Reset Derivative d PI τ - PID 2τ t K(2ε t d ) 2 2τ t d K(2ε t d ) τ t d t d 2 τt d 2τ t K=Process Gain, t d =Dead time τ ε =Time Constant =Desired Closed Loop Response d! 16! Integral Process Gain Reset Derivative P - - PI 2 - PID 1 Kε Kε td 2ε 2 td K( ε) 2 2 ε2 td 2ε 2 t d 2

PID Tuning The Advanced Tuning window is for user to perform detail analysis of each step test data and confirm the final suitable P, I, D parameters. Loop Details Pane most of the important parameters in loop configuration Step Pane the list of steps captured under the selected tag and the preview of the step data Loops Pane displays loops grouped by the Location defined in Loop Configuration the main window that user does the analysis for model and loop simulation Advanced Tuning Pane! 17!

PID Tuning is always correct?! 18!

Research & Development in the Future Plant Life Cycle Monitoring & Diagnosis! 19!

Loop Oscillation & Valve Stiction Dianosis Valve Stiction Results: Oscillating Only! 20!

Loop Oscillation & Valve Stiction Diagnosis Valve Stiction Results: Oscillating & Sticking! 21!

What is problem after installation? Industry has implemented many projects Shift from project work towards maintenance Staff is less appealed by maintenance work Shortage of skilled staff in process control and optimisation Maintenance can be tedious and time consuming Too much focus towards Uptime (Online factor) Applications do not deliver optimum performance Reference : - Recent survey of 20,000 loops performance Excellent 16% Acceptable 12% Fair 28% Poor 11% Manual mode 33%! 22!

Thank you for your attention! 23!