CHE 185 – PROCESS CONTROL AND DYNAMICS

Slides:



Advertisements
Similar presentations
Stability Margins Professor Walter W. Olson
Advertisements

Dynamic Behavior of Closed-Loop Control Systems
Chapter 4 Continuous Time Signals Time Response Continuous Time Signals Time Response.
Chapter 10 Stability Analysis and Controller Tuning
Nyquist Stability Criterion
Chapter 10: Frequency Response Techniques 1 ©2000, John Wiley & Sons, Inc. Nise/Control Systems Engineering, 3/e Chapter 10 Frequency Response Techniques.
Frequency Response Techniques
Lecture 8B Frequency Response
Loop Shaping Professor Walter W. Olson
4. System Response This module is concern with the response of LTI system. L.T. is used to investigate the response of first and second order systems.
T S R Q R Q = (R(ST) | ) | = (R(SQ) | ) | T S R Q CEC 220 Revisited.
CHE 185 – PROCESS CONTROL AND DYNAMICS
CHE 185 – PROCESS CONTROL AND DYNAMICS
Quiz: Find an expression for in terms of the component symbols.
4.3. Time Response Specification in Design
Control System Design Based on Frequency Response Analysis
Frequency Response Methods and Stability
Transient & Steady State Response Analysis
Lecture 9: Compensator Design in Frequency Domain.
Dr. / Mohamed Ahmed Ebrahim Mohamed Automatic Control By Dr. / Mohamed Ahmed Ebrahim Mohamed Web site:
Professor Walter W. Olson Department of Mechanical, Industrial and Manufacturing Engineering University of Toledo Loop Transfer Function Real Imaginary.
Out response, Poles, and Zeros
Feedback Control Systems (FCS) Dr. Imtiaz Hussain URL :
Control System Design Based on Frequency Response Analysis
Automatic Control Theory-
1 Chapter 2 We need to write differential equations representing the system or subsystem. Then write the Laplace transform of the system. Then we will.
Chapter 13 1 Frequency Response Analysis Sinusoidal Forcing of a First-Order Process For a first-order transfer function with gain K and time constant,
Chapter 8 Frequency-Response Analysis
Course Review Part 3. Manual stability control Manual servo control.
Professor Walter W. Olson Department of Mechanical, Industrial and Manufacturing Engineering University of Toledo Loop Shaping.
Chapter 14 Frequency Response Force dynamic process with A sin  t, Chapter
Chapter 5 Transient and Steady State Response “I will study and get ready and someday my chance will come” Abraham Lincoln.
1 Chapter 5 Sinusoidal Input. 2 Chapter 5 Examples: 1.24 hour variations in cooling water temperature Hz electrical noise (in USA!) Processes are.
Fundamentals of PWM Dc-to-Dc Power Conversion Dynamic Performance of PWM Dc-to-Dc Converters.
Frequency Response OBJECTIVE - Bode and Nyquist plots for control analysis - Determination of transfer function - Gain and Phase margins - Stability in.
Chapter 10 Frequency Response Techniques Frequency Response Techniques.
Chapter 3 Dynamic Response The Block Diagram Block diagram is a graphical tool to visualize the model of a system and evaluate the mathematical relationships.
INC 341PT & BP INC341 Frequency Response Method Lecture 11.
Lecture 22: Frequency Response Analysis (Pt II) 1.Conclusion of Bode plot construction 2.Relative stability 3.System identification example ME 431, Lecture.
Frequency Response Analysis and Stability
Lecture 7 Poles and Zeros Stability. Transfer Function Models General Representation wh where z i are the zeros p i are the poles n ≥ m to have a physically.
ChE 182 Chemical Process Dynamics and Control
G(s) Input (sinusoid) Time Output Ti me InputOutput A linear, time-invariant single input and single output (SISO) system. The input to this system is.
1 Time Response. CHAPTER Poles and Zeros and System Response. Figure 3.1: (a) System showing input and output; (b) Pole-zero plot of the system;
Dr. Tamer Samy Gaafar Lec. 2 Transfer Functions & Block Diagrams.
SKEE 3143 Control Systems Design Chapter 2 – PID Controllers Design
System Dynamics Dr. Mohammad Kilani
Feedback Control System THE ROOT-LOCUS DESIGN METHOD Dr.-Ing. Erwin Sitompul Chapter 5
EE4262: Digital and Non-Linear Control
Automatic Control Theory CSE 322
Time Domain and Frequency Domain Analysis
Automatic control systems I
Nyguist criterion Assist. Professor. Dr. Mohammed Abdulrazzaq.
Automatic Control Theory CSE 322
Time Response Analysis
DNT Control Principle Frequency Response Techniques DNT Control Principle.
Frequency-Domain Analysis and stability determination
Bode Plot Nafees Ahmed Asstt. Professor, EE Deptt DIT, DehraDun.
Control System Analysis and Design by the Frequency Response Method
Digital Control Systems (DCS)
Frequency Response Techniques
Hanani binti Abdul Wahab 24 September 2008
Frequency Response Techniques
Nyquist Stability Criterion
Frequency Response Method
Frequency Domain specifications.
7-5 Relative Stability.
Chapter 4. Time Response I may not have gone where I intended to go, but I think I have ended up where I needed to be. Pusan National University Intelligent.
Frequency Response Techniques
The Frequency-Response Design Method
Presentation transcript:

CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS

Frequency Response Analysis Is the response of a process to a sinusoidal input Considers the effect of the time scale of the input. Important for understanding the propagation of variability through a process. Important for terminology of the process control field. But it is NOT normally used for tuning or design of industrial controllers.

Frequency Response Analysis Process Exposed to a Sinusoidal Input.

Frequency Response Analysis Key Components – INPUT FREQUENCY, ampLitude ratio, phase angle.

Frequency Response Analysis Effect of Frequency on Ar and Φ PEAK TIME DIFFERENCE Φ= 𝜔 ∆ 𝑡 𝑝 2𝜋 360 °

Frequency graphics Bode plot of Ar and Φ versus frequency ω

BODE STABILITY PLOT BASIS OF BODE PLOT IS A MEASURE OF RELATIVE AMPLITUDE AND PHASE LAG BETWEEN A REGULAR (SINUSOIDAL) SET POINT CHANGE AND THE OUTPUT SIGNAL THIS TECHNIQUE INDICATES STABILITY OF THE SYSTEM THE ANALYSIS IS COMPLETED WITH AN OPEN LOOP

BODE GENERATION Direct excitation of process. Ways to Generate Bode Plot INCLUDE: Direct excitation of process. Combine transfer function of the process with sinusoidal input. Substitute s=i w into Gp(s) and convert into real and imaginary components which yield Ar(w) and f(w). SEE APPLICATION METHOD IN EXAMPLES 11.1 AND 11.2 Apply a pulse test.

BODE STABILITY PLOT A SINUSOIDAL SETPOINT IS SENT TO THE LOOP AFTER THE SYSTEM REACHES STEADY STATE, THERE IS A LAG, CALLED THE PHASE LAG, BETWEEN THE AMPLITUDE PEAK OF THE INLET SIGNAL AND THE AMPLITUDE PEAK OF THE OUTLET SIGNAL THE FREQUENCY IS ADJUSTED SO THE PHASE LAG OF THE OUTLET SIGNAL IS 180° BEHIND THE INPUT SIGNAL

BODE STABILITY PLOT THE RESULTS ARE THEN APPLIED TO A CLOSED LOOP THE SETPOINT IS CHANGED TO A CONSTANT VALUE SINCE THE ERROR SIGNAL IS 180° OUT OF PHASE AND IS NEGATIVE RELATIVE TO THE INPUT SIGNAL, IT REINFORCES THE PREVIOUS ERROR SIGNAL

BODE STABILITY PLOT THE AMPLITUDE OF THE ERROR SIGNAL BECOMES THE OTHER FACTOR IF THE AMPLITUDE OF THE ERROR SIGNAL TO THE AMPLITUDE OF THE ORIGINAL SINUSOID SETPOINT, CALLED THE AMPLITUDE RATIO, IS LESS THAN ONE THEN THE ERROR WILL DECAY TO ZERO OVER TIME, IF THE AMPLITUDE RATIO WAS EQUAL TO ONE, A PERMANENT STANDING WAVE WILL RESULT IF THE AMPLITUDE RATIO WAS GREATER THAN ONE, THE ERROR WILL GROW WITHOUT LIMIT.

BODE STABILITY PLOT BODE’S STABILITY CRITERION SAYS: WHEN THE AMPLITUDE RATIO IS LESS THAN ONE, THE SYSTEM IS STABLE WHEN THE AMPLITUDE RATIO IS GREATER THAN ONE, THE SYSTEM IS UNSTABLE THE AMPLITUDE RATIO IS DEFINED AS: WHERE ar REFERS TO AMPLITUDE AS SHOWN IN FIGUREs 11.2.1 and 11.2.2 IN THE TEXT AND ω IS THE FREQUENCY OF THE SINUSOID

BODE STABILITY PLOT BODE PLOTS GENERAL TECHNIQUE TO PLOT THESE ARE SHOWN FOR FOPDT PROCESSES IN FIGURES 11.2.2 AND 11.3.2 A SECOND ORDER PLOT IS FIGURE 11.3.3 GENERAL TECHNIQUE TO PLOT Write the transfer function in proper form (unit value for lowest order term in denominator) Separate the transfer function into parts based on poles and zeros Draw bode diagram for each part Sum the parts to get the final plot

Bode Plot creation example (http://lpsa. swarthmore Transfer function in proper form 𝐻 𝑠 = 100 𝑠+30 or 𝐻 𝑠 =3.3 1 𝑠 30 +1 Parts are based on pole at s=30 and constant of 3.3 Pole plot is constant 0 db up to break ω, then drops off Constant has value of 10.4 db

Bode Plot creation example (http://lpsa. swarthmore Function with real poles and zeros

Bode Plot creation example (http://lpsa. swarthmore Function with real poles and zeros

Bode Plot creation example (http://lpsa. swarthmore Function with pole at origin

Bode Plot creation example (http://lpsa. swarthmore Function with repeated real poles, negative constant

Bode Plot creation example (http://lpsa. swarthmore Function with complex conjugate poles

Bode Plot creation example (http://lpsa. swarthmore Function with multiple poles at origin, complex conjugate zeros

Bode Plot creation example (http://lpsa. swarthmore Function with multiple poles at origin, complex conjugate zeros

Bode Plot creation example (http://lpsa. swarthmore Function with time delay

BODE STABILITY PLOT Developing a Bode Plot from the Transfer Function

BODE STABILITY PLOT Derivation for a First Order Process

BODE STABILITY PLOT Properties of Bode Plots

BODE STABILITY PLOT Bode Plot of Complex Transfer Functions Break transfer function into a product of simple transfer functions. Identify Ar(ω) and Φ(ω) of each simple transfer function from Table 11.1. Combine to get Ar(ω) and Φ(ω) for complex transfer function according to properties. Plot results as a function of ω.

BODE STABILITY PLOT BODE PLOTS CAN BE PLOTTED FROM TRANSFER FUNCTIONS WE CAN SET UP THE TRANSFER FUNCTION: Y(s) – Gp(s)C(s) WHERE C(s) IS THE SINUSOIDAL INPUT AN INVERSE LaPLACE TRANSFORM OF THE RESULT THEN PROVIDES A TIME FUNCTION

BODE STABILITY PLOT TAKING THIS TO A LIMIT TO ELIMINATE TRANSIENTS THAT WILL DECAY LEAVES THE STANDING WAVE FUNCTION THIS CAN BE USED TO EVALUATE Ar AS A FUNCTION OF ω AND φ AS A FUNCTION OF ω TABLE 11.1 PROVIDES FUNCTIONS TO CALCULATE Ar AND φ FOR A NUMBER OF COMMON TRANSFER FUNCTIONS

BODE STABILITY PLOT GAIN MARGIN AND PHASE MARGIN THE BODE STABILITY CRITERION IS EVALUATED AT THE POINT WHERE φ IS EQUAL TO -180°. THE FREQUENCY AT THIS POINT IS CALLED THE CRITICAL FREQUENCY

BODE STABILITY PLOT GAIN MARGIN AND PHASE MARGIN THE VALUE OF Ar CALCULATED AT THE CRITICAL FREQUENCY, Ar* DETERMINES THE PROCESS STABILITY THIS IS EXPRESSED AS THE GAIN MARGIN: WHEN GM > 1, THE SYSTEM IS STABLE

BODE STABILITY PLOT GAIN MARGIN AND PHASE MARGIN THE PHASE MARGIN IS THE VALUE OF THE PHASE ANGLE AT THE POINT WHERE Ar = 1 AND IS RELATIVE TO THE PHASE ANGLE OF -180°: (EQUATION 11.3.2) THE FREQUENCY WHERE THIS CONDITION OCCURS IS CALLED THE CROSSOVER FREQUENCY

BODE STABILITY PLOT PULSE TEST THIS IS AN OPEN LOOP TEST USED TO OBTAIN THE VALUES NECESSARY TO CREATE A BODE PLOT RESULTS COMPARE THE AMPLITUDE AND THE DURATION TIMES FOR THE INPUT AND OUTPUT VALUES FOR AN OPEN LOOP. THESE ARE USED WITH EQUATIONS 11.4.1 THROUGH 11.4.8 TO OBTAIN THE BODE PLOT

BODE STABILITY PLOT PULSE TEST EXAMPLE

BODE STABILITY PLOT Developing a Pulse Test Process Transfer Function

BODE STABILITY PLOT Limitations of Transfer Functions Developed from Pulse Tests They require an open loop time constant to complete. Disturbances can corrupt the results. Bode plots developed from pulse tests tend to be noisy near the crossover frequency which affects GM and PM calculations.

NYQUIST DIAGRAM PULSE TEST COMBINES THE VALUE OF Ar AND φ ON A SINGLE DIAGRAM OTHERWISE IT HAS NO ADVANTAGE OVER THE BODE PLOTS

Closed Loop Frequency Response REFERENCE FIGURE 11.6.1

Example of a Closed Loop Bode Plot REFERENCE FIGURE 11.6.2

Analysis of Closed Loop Bode Plot REFERENCE FIGURE 11.6.2 At low frequencies, the controller has time to reject the disturbances, i.e., Ar is small. At high frequencies, the process filters (averages) out the variations and Ar is small. At intermediate frequencies, the controlled system is most sensitive to disturbances. The peak frequency indicates the frequency for which a controller is most sensitive.