Constant pressure air charging cascade control system based on fuzzy PID controller. Jun Zhao & Zheng Zhang

Similar documents
Optimization of Air compressor Motor speed for Reducing Power Consumption

Fail Operational Controls for an Independent Metering Valve

Application of CHE100 in Frequency Conversion Alteration of Air Compressor System

Air Compressor Control System for Energy Saving in Manufacturing Plant

Process Control Loops

Unit 55: Instrumentation and Control Principles

Application Block Library Fan Control Optimization

Predictive Control of Dissolved Oxygen Concentration in Cynoglossus Semilaevis Industrial Aquaculture

Folding Reticulated Shell Structure Wind Pressure Coefficient Prediction Research based on RBF Neural Network

Fail operational controls for an independent metering valve

Characterizers for control loops

67. Sectional normalization and recognization on the PV-Diagram of reciprocating compressor

STICTION: THE HIDDEN MENACE

Programmable Valves Enable Both Precision Motion Control and Energy Saving

CHEMICAL ENGINEERING LABORATORY CHEG 239W. Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller

RICK FAUSEL, BUSINESS DEVELOPMENT ENGINEER TURBOMACHINERY CONTROL SYSTEM DESIGN OBJECTIVES

PROCESS DYNAMIC AND CONTROL MODIFIED II QUADRUPLE TANK ON LABVIEW APPLICATION

Workshop 302-compressor-anti-surge

CONTROL and INSTRUMENTATION

NATIONAL UNIVERSITY OF SINGAPORE. EE3302/EE3302E Industrial Control Systems E1: ADVANCED CONTROL SYSTEMS

THE PRESSURE SIGNAL CALIBRATION TECHNOLOGY OF THE COMPREHENSIVE TEST

Exercise 8. Closed-Loop Pressure Control, Proportional-Plus-Integral Mode EXERCISE OBJECTIVE

PI control for regulating pressure inside a hypersonic wind tunnel

Compensator Design for Speed Control of DC Motor by Root Locus Approach using MATLAB

The Future of Hydraulic Control in Water-Systems

Digital Level Control One and Two Loops Proportional and Integral Control Single-Loop and Cascade Control

2600T Series Pressure Transmitters Plugged Impulse Line Detection Diagnostic. Pressure Measurement Engineered solutions for all applications

WMO LABORATORY INTERCOMPARISON OF RAIN INTENSITY GAUGES

Gerald D. Anderson. Education Technical Specialist

Dynamic Operation of a 4 K Pulse Tube Cryocooler with Inverter Compressors

Instrumentation (and

CHARACTERISTICS OF LEAK DETECTION BASED ON DIFERENTIAL PRESSURE MEASUREMENT

Hydronic Systems Balance

Measuring range Δp (span = 100%) Pa

RESEARCH OF BLOCKAGE SEGMENT DETECTION IN WATER SUPPLY PIPELINE BASED ON FLUID TRANSIENT ANALYSIS ABSTRACT

Computer Aided Drafting, Design and Manufacturing Volume 26, Number 2, June 2016, Page 53. The design of exoskeleton lower limbs rehabilitation robot

GP1 & GP2. Electropneumatic Regulators FOR PRESSURE CONTROL TO 1,000 PSI

Mitos Fluika Pressure and Vacuum Pumps Datasheet

Basketball field goal percentage prediction model research and application based on BP neural network

V10K GAS FEED SYSTEM WALLACE & TIERNAN PRODUCTS

AN ANALYSIS ON HIGH PRESSURE DYNAMIC CALIBRATORS USED IN THE DEFENSE AREAS

How to Combat Process Disturbances and Interactions

The Effect Analysis of Rudder between X-Form and Cross-Form

Sizing Pulsation Dampeners Is Critical to Effectiveness

u = Open Access Reliability Analysis and Optimization of the Ship Ballast Water System Tang Ming 1, Zhu Fa-xin 2,* and Li Yu-le 2 " ) x # m," > 0

Wind Tunnel Instrumentation System

Author s Name Name of the Paper Session. Positioning Committee. Marine Technology Society. DYNAMIC POSITIONING CONFERENCE September 18-19, 2001

Exercise 2-2. Second-Order Interacting Processes EXERCISE OBJECTIVE DISCUSSION OUTLINE. The actual setup DISCUSSION

Introduction to Pneumatics

Guideline No.M-05(201510) M-05 AIR COMPRESSOR. Issued date: 20 October China Classification Society

Experimental Investigation on Transient Response of Two Stage Pressure Relief Valve

UNIVERSITY OF WATERLOO

Micro Cold Gas Proportion thruster for Deep Interplanetary Exploration Development in BICE

Coriolis Mass Flow Meter

Pressure on Demand. Air Pressure Amplifiers

PIG MOTION AND DYNAMICS IN COMPLEX GAS NETWORKS. Dr Aidan O Donoghue, Pipeline Research Limited, Glasgow

Development of Large Capacity CO2 Scroll Compressor

Level Process Control. Penn State Chemical Engineering

Unit 24: Applications of Pneumatics and Hydraulics

ENS-200 Energy saving trainer

Industrial Compressor Controls Standard Custom

Lab 4: Root Locus Based Control Design

The Compact, Portable, Efficient and Economical Solution to boost Shop Compressed Air Pressure by 2 or 3 times

Acoustical Modeling of Reciprocating Compressors With Stepless Valve Unloaders

Introductions for a Multi-function Portable SF 6 Leaking Alarm Testing Device Based on a Two-level Configure Gas Technology

Air Amplifiers & SYSTEMS

Research of Intelligent Control of Air Compressor at Constant Pressure

Model 4000 Pressure Controller

2. Determine how the mass transfer rate is affected by gas flow rate and liquid flow rate.

A Fault Diagnosis Monitoring System of Reciprocating Pump

SRL Series. Oil-less Scroll Air Compressors. Pharmaceutical. Research & Development. Food & Beverage. Chemical. Electronic

Multiple Pressure Booster Systems With Variable Speed Controller Type BL

EXPERIMENT 2 LEVEL CONTROL SYSTEM

Hydraulic and Economic Analysis of Real Time Control

SF SERIES CNG COMPRESSOR MODEL HF-4MH. 4 Nm3/Hour Displacement OPERATION MANUAL

Multivariable Predictive Control and its Application on the Solvent Dehydration Tower

Research on the Sealing Detection Technology for No Leak Detection Interface Specimen Yingjun Huanga, Xudong Liaob, Guoyun Baic, Tao Chend, Miao Loue

SPH 4C Unit 4 Hydraulics and Pneumatic Systems

Fisher 2625 and 2625NS Volume Boosters

TESTING OF BELIMO PRESSURE INDEPENDENT CHARACTERIZED CONTROL VALVES

COMPRESSED AIR DISTRIBUTION SYSTEMS

Journal of Chemical and Pharmaceutical Research, 2016, 8(6): Research Article. Walking Robot Stability Based on Inverted Pendulum Model

S-CO 2 Brayton Recompression Loop Design and Control

A Depletion Compensated Wet Bath Simulator For Calibrating Evidential Breath Alcohol Analyzers

Correction of Pressure Drop in Steam and Water System in Performance Test of Boiler

Ballorex Dynamic Description. Versions. Benefits. Balancing

International Research Journal of Electronics and Computer Engineering Vol 1(3) Oct-Dec 2015

MANUAL KPS Pressure Control Valve

Analysis and Research of Mooring System. Jiahui Fan*

CONTROL VALVE TESTING

AIR DRIVEN. Gas Boosters & SYSTEMS. Accepting VISA, MasterCard and American Express

A Distributed Control System using CAN bus for an AUV

LUGB Vortex Flowmeter

CT433 - Machine Safety

Specifications and information are subject to change without notice. Up-to-date address information is available on our website.

Test Method of Trap Performance for Induced Siphonage

Special Print. Innovative Control Technology. Control Valves with Extremely Fast and Precise Positioning Capabilities

Plant, components and devices for very high and high pressures (7000 bar and over)

WATER HYDRAULIC HIGH SPEED SOLENOID VALVE AND ITS APPLICATION

P-5215 Differential Pressure Transmitter

Transcription:

International Conference on Applied Science and Engineering Innovation (ASEI 2015) Constant pressure air charging cascade control system based on fuzzy PID controller Jun Zhao & Zheng Zhang College of information science and engineering Wuhan University of science and technology Wuhan 430081 China Keywords: Fuzzy PID control; Constant pressure air charging; Pneumatic gas booster; Cascade control. Abstract. Aiming at the problem of air charging safe high efficient and energy-saving with pneumatic gas booster a constant pressure air charging system was designed to rapid filling respirator and the fire respirator`s com-pressed air bottle fast filling station was transformed into air charging experiment platform the controller combined the cascade control principle of fuzzy control and conventional PID control algorithm and realized the Real-time adjustment of the PID parameters by automatically adjusting the pressure of pneumatic gas booster`s drive circuit to realize automatic air charging in a constant pressure.the simulation and experiment results show that the system has a very good dynamic static performance and the actual control effect it pro-vided a realization method of constant pressure air charging gas booster. 1. Introduction Fire respirator`s compressed air bottle fast filling station is an inflation equipment for air respirator. It is widely used in petroleum chemical marine fire smelting factories and mines etc. In long time fire operations firefighters who entered the anoxic toxic harmful gases and etc. fire rescue scene need to consume large amounts of compressed breathing air supply. Restricted by the max number of air respirators that can be configured it is required that the fire respirator`s compressed air bottle fast filling station can inflate the respirators under a safe pressure value fast safe clean and efficiently thus ensues the smooth progress of the fire-fighting tas. At present the design and application of constant pressure inflation system has attracted widespread attention. In general classified by the types of gas supercharging equipment there are two inds of inflation systems: one is the constant pressure inflation systems based on electric-drive gas supercharging equipment. Zhu Yinghuang Yao Shiuan et al. renovated the traditional compressor by constant pressure variable frequency technique using frequency converter with conventional PID control method which extends the life span of equipment achieves energy saving and ensures the stability of the pipe networ. Wang Jinghui et al. designed a constant pressure gas supplying compressor system based on fuzzy control which improves the reliability and stability of the system. Bai Kunhai Qu Xusheng et al. who designed the fuzzy-pid control system by combining the principle of the fuzzy control and conventional PID control and verify its superiority. Cai Kailong et al. proposed an adaptive PID controller based on neural networ which controls the pressure of constant pressure gas supplying system by stepper motor. The other is the constant pressure inflation system based on gas-drive supercharging equipment which is used in places with a high-pressure gas source such as large ships. Compared with system using electric-drive supercharging equipment system using gas-drive supercharging equipment does not produce heat spars need no external lubricants can start and stop continuously which is light reliable and easy to maintain. Faced with constant pressure inflation system using gas-drive supercharging equipment the algorithm above has certain limitations. With the increasingly use of inflatable devices based on gas-drive supercharging equipment it has a very important application value to design safe and energy-saving constant pressure automatic inflation system. This paper studies on compressed air fast inflating station for cylinders of fire-fighting respirators based on gas-drive supercharging equipment which applied to large ships. According to the gas-drive 2015. The authors - Published by Atlantis Press 1357

gas booster pump s nonlinear large time delay characteristics the inflatable constant pressure cascade control system based on fuzzy PID's is designed. This system realizes constant-pressure stable safe fast inflation of a plurality of high-pressure gas cylinders by adjusting the driving pressure of the gas booster pump automatically. Fire respirator`s compressed air bottle fast filling station was transformed into air charging experiment platform which is used to verify the effectiveness and superiority of the fuzzy PID cascade control algorithm. 2. Design OF Constant pressure air charging cascade control system 2.1 Control program design of constant pressure air charging system Constant pressure air charging system is a system of inflation pressure control this system is required to filling 1-4 6.8L respirator as soon as possible and at the same time to prevent the gas bottle mouth be filled with explosive hazards etc. It`s main objective is control the inflate pressure under a safe value (30Mpa) after gas booster started and automatically stop charging when the cylinder respirator`s pressure increased to 30Mpa. According to the technological requirements design of Schematic diagram of the control system as shown in figure 1: Figure 1.Schematic diagram of the control system. 2.2 Air charging process design In order to achieve high efficiency and energy saving the whole process is divided into two stage natural air charging stage and booster air charging stage. The first stage is natural air charging stage. Mae full use of high pressure gas source(about 10Mpa) it`s much larger than the respirator`s pressure(approximately 6Mpa) this stage is not enabled pneumatic gas booster just open electric shut-off valve and direct inflatable via Inflatable loop bypass. At the same time as the air pressure between respirator and high pressure gas source get smaller inflatable process get slower when the pressure difference reaches a given pressure value end natural air charging stage. The second stage is booster air charging stage. After natural air charging stage constant pressure air charging system automatically shut down the electric shut-off valve and turn on electric pressure regulator valve by adjusting the Drive gas source pressure to achieve constant pressure inflate. 2.3 Cascade Control System Design At the booster air charging stage constant pressure air charging system maintained the inflate pressure at a safe value (30Mpa) through adjusting the drive air pressure. If use the exports (inflate) pressure as the main signal bac to the controller the controller directly controls the electric pressure regulating valve this single-loop control system shows its poor control performance it is difficult to obtain better control quality. The reason is that the electric valve and the gas booster have a long distance and the driving pressure need time to regulate. Export (inflate) pressure lag and large inertia long time delay could easily lead to control is not timely the overshoot increases and stability. Therefore in order to improve the system response speed improve the control quality use the driving 1358

pressure as the auxiliary control signals and design pressure-pressure air charging cascade control system structure of the cascade control system as shown in Figure 2: Figure 2.Structure of the cascade control system. The purpose of the master controller is to control the gas booster pump outlet (inflatable) pressure. When there is a deviation of the inflation pressure and the set value of the actual inflation pressure detection automatic control algorithm on the main controller calculates a control output the control output that is a given sub-controllers. Practice and experience shows that the constant pressure inflation system is a complex system of nonlinear large delay. Conventional PID controller tuning parameters are often poor poor performance poor adaptability of the controlled process; fuzzy controller is not required to master the mathematical model of controlled object but it is generally not high control accuracy. So the master controller using fuzzy control and PID control methods combine the two weanesses both fuzzy control and flexible adaptable PID control also has the advantages of high accuracy. Secondary loop is a servo system it's a given value varies with changes in the master controller output. In order to drive the output pressure of the master controller to quicly follow and remain stable given deputy controller preferably without integral role because the integral action will slow trac; the derivative action is not needed as deputy controller When the derivative action once the master controller and a slight change in the output of the electric valve will change dramatically and this control is unfavorable. In this system the sub-controllers just using P control algorithm can achieve a good result. 3. Fuzzy PID controller design 3.1 Fuzzy PID control theory Fuzzy PID controller is mainly composed by two parameters PID controller and fuzzy inference section. Fuzzy controller select pressure error e and pressure error change rate e as input; and three parameters proportion: P integration: i differential: d as output. Through fuzzy inference to adjust the parameters KP KI KD online as the e and e changed. So that the controlled object has a good dynamic and static performance. Fuzzy PID controller structure as show in Figure 3: Figure 3.Structure of the fuzzy PID controller. 3.2 Fuzzy sets and membership Fuzzy controller input output basic discourse domain: e discourse domain [-11]; 1359

e discourse domain [-0.10.1]; P discourse domain [-0.20.2]; i discourse domain [-0.050.05]; d discourse domain [-0.020.02] The fuzzy domain unified as [-6 6]. Fuzzy set is unified to {NB NM NS Z PS PM PB} were negative negative negative zero is small middle large. Select the trigonometric function as membership function of E and E. x a x ( a b) u( x ) = b a x c x ( a b) b c The parameters of a and b values from -6 to 6. Select normal distribution function as membership function of P i and d. 2 ( x x0 ) 2 2 δ u( x) = e The δ is the standard deviation. 3.3 Fuzzy control rules According to the different fuzzy quantization value of e and e analysis and summary of control rules are as follows: (1) When E have large values large selection of Kp to speed up the system response in order to prevent the super harmonic and differential overflow select a small Ki and Kd is zero. (2)When E have medium size values in order maes the system has a small super harmonic choose a small Kp a moderate Ki can guarantee the response speed Kd have a greater impact on the system so select a small Kd. (3) When E is relatively small in order to ensure the good steady state performance of the system select the larger Ki and larger Kp. At the same time in order to avoid system oscillation near the set point and improve the anti-interference ability of the system when E have large values select smaller Kd; when E have small values select larger Kd. 3.4 Defuzzification Defuzzification using method of the weighted average method the calculation formula is as follows: y m 1 = m xi u( xi ) u( x ) 1 i X i represents an element in the domain of fuzzy theory u(x i ) represents its membership degree value of m represents fuzzy membership is not the number 0. Get the value of Kp Ki and Kd through the weighted average method. The output of fuzzy controller: p = K K p P i = K K i i = K K d d d Among them K K p K i and d is quantification factor of P i and d. 0.2 0.05 K p = = 0.0333 K = = 0. 0083 6 i 6 0.02 K d = = 0.0033. 6 So the final parameter values for the PID control: p = p0 + P i = i 0 + i d = d 0 + d 1360

Among them p0 i0 K D0 as the PID controller by the original value site commissioning experience. 4. Simulation and experimental results Pneumatic gas booster start with the initial state and then inflate the pipe networ with constant pressure the inflatable pressure stabilize after the two processes: (1) Pneumatic gas booster gradually sent gas to the pipe networ and this is a lag in the process; (2)Gas is gradually filled the pipe networ gas pressure gradually increased until stability which is a process of inertia. So according to the practice and experience can be said that the mathematical model of pneumatic gas booster and electric valve are equivalent to one order inertia and pure lag system its transfer τs Ke function: Gs = Ts + 1. After identification the parameters of the mathematical model of gas booster pump: K=21 T=38 =5.7. Parameters of electric valve mathematical model: K=1.3 T=8 =2.6. Set the initial parameters of PID: P=0.5 i=0.002 d=0.8. The constant pressure air charging cascade control system simulation model establish by using Simulin and fuzzy control box in MATLAB as shown in figure 4. Figure 4.Simulation model System simulation of the response curve as shown in Figure 5 the curves of the 1 output for cascade control based on fuzzy PID curve of 2 output for single loop control system fuzzy PID control curves 3 of output for traditional control system based on PID. As can be seen from Figure 5 compared with the traditional PID control fuzzy PID control has faster response produced only minimal overshoot faster at steady state. The cascade control based on fuzzy PID relative to the fuzzy PID based on single loop control has faster response better control effect. The actual inflation experiment results are shown in Table 1 we can see that the constant pressure air charging cascade control system based on fuzzy PID controller can inflatable 4 6.8L respirators in 5 minutes and the charging time relative to the fuzzy PID control is reduced by 13% can be very good to meet the actual demand of filling respirator s. Figure 5.The simulation results 1361

Number of respirator Table 1.The result of air charging experiment Cascade control based on fuzzy PID fuzzy PID 5. Summary 1 1.259 min 1.508 min 2 2.617 min 3.015 min 4 5.235 min 6.030 min Point at the fire respirator`s compressed air bottle fast filling station based on pneumatic gas booster designed a constant pressure air charging cascade control system based on fuzzy PID controller through full use of the high pressure gas source the natural air charging stage achieved a good energy saving effect. The simulation results show that the method can play the advantages of fuzzy control PID control and cascade control. The system can be stabilized in a shorter period of time smaller overshoot and effectively eliminating adverse effects of large delay large inertia and high pressure gas source fluctuation to system during the charging process and achieved the purpose of security efficient. References [1] Bai Kunhai. 1974. Design of constant pressure supply air system based on fuzzy PID. Chinese Hydraulics & Pneumatics 2012 (6):53-55. [2] Cai Kailong. 1979. Application of neural networ PID control in constant pressure air feeding system based on step motor. Chinese Hydraulics & Pneumatics 2006 (6):63-66. [3] Wang Jinhui. 1978. Fuzzy control-based constant pressure centroi for air compressors. Control and Instruments in Chemical Industry 2011 38(6):689-690. [4] Zhu Yinghuang. 1967. Application of frequency inverter in constant pressure control of air compressor. Process Automation Instrumentation 2009 30(1):66-69. [5] Zhai Shiuan. 1979. Inverter in transformation of air compressorconstant pressure air supply. Electric Machines & Control Application 2012 39(3):40-43. [6] Zhai Xusheng. 1984. A constant pressure feeding system based on adaptive fuzzy PID control. Chinese Hydraulics & Pneumatics 2008 (2):21-23. 1362