Dynamic Behavior Chapter 5

Slides:



Advertisements
Similar presentations
CHE 185 – PROCESS CONTROL AND DYNAMICS
Advertisements

The Performance of Feedback Control Systems
Dynamic Behavior of Closed-Loop Control Systems
Chapter 4 Continuous Time Signals Time Response Continuous Time Signals Time Response.
Dynamic Behavior Chapter 5 In analyzing process dynamic and process control systems, it is important to know how the process responds to changes in the.
Dynamic Behavior Chapter 5
4.3. Time Response Specification in Design
Laplace Transforms Important analytical method for solving linear ordinary differential equations. - Application to nonlinear ODEs? Must linearize first.
Transfer Functions Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: The following terminology.
Transfer Functions Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: The following terminology.
Frequency Response Analysis
Transient & Steady State Response Analysis
Chapter 3 1 Laplace Transforms 1. Standard notation in dynamics and control (shorthand notation) 2. Converts mathematics to algebraic operations 3. Advantageous.
Out response, Poles, and Zeros
Feedback Control Systems (FCS) Dr. Imtiaz Hussain URL :
1 Dynamic Behavior Chapter 5 In analyzing process dynamic and process control systems, it is important to know how the process responds to changes in the.
1 On Free Mechanical Vibrations As derived in section 4.1( following Newton’s 2nd law of motion and the Hooke’s law), the D.E. for the mass-spring oscillator.
Transfer Functions Chapter 4
MESB374 System Modeling and Analysis Forced Response
DYNAMIC BEHAVIOR AND STABILITY OF CLOSED-LOOP CONTROL SYSTEMS
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,
DYNAMIC BEHAVIOR OF PROCESSES :
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.
Chapter 4 Dynamic Systems: Higher Order Processes Prof. Shi-Shang Jang National Tsing-Hua University Chemical Engineering Dept. Hsin Chu, Taiwan April,
Transfer Functions Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: The following terminology.
Lec 6. Second Order Systems
ERT 210/4 Process Control & Dynamics DYNAMIC BEHAVIOR OF PROCESSES :
DYNAMIC BEHAVIOR OF PROCESSES :
Control engineering ( ) Time response of first order system PREPARED BY: Patel Ravindra.
Class 3 Linear System Solution Using the Laplace Transform
System Dynamics Dr. Mohammad Kilani
Lecture 7/8 Analysis in the time domain (II) North China Electric Power University Sun Hairong.
Transfer Functions Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: The following terminology.
Automatic Control Theory CSE 322
Lesson 20: Process Characteristics- 2nd Order Lag Process
Laplace Transforms Chapter 3 Standard notation in dynamics and control
Youngjune, Han Chapter 4 Time Response Youngjune, Han
Control Response Patterns
Transfer Functions Chapter 4
Time Response Analysis
CHAPTER VI BLOCK DIAGRAMS AND LINEARIZATION
Dynamic Behavior Chapter 5
Instructor: Jongeun Choi
Dynamic Behavior of Ideal Systems
Dynamic Behavior Chapter 5
Frequency Response Analysis
G1 and G2 are transfer functions and independent of the
UNIT-II TIME RESPONSE ANALYSIS
Important Properties of Laplace Transforms
Control Response Patterns
UNIVERSITI MALAYSIA PERLIS SCHOOL OF ELECTRICAL SYSTEM ENGINEERING
First-Order System Chapter 5
Mechatronics Engineering
Solution of ODEs by Laplace Transforms
Response of Higher Order Systems
Frequency Response Analysis
Interacting vs. Noninteracting Systems
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.
Control System Toolbox (Part-II)
Second-Order Systems Chapter 5 Standard form:
Frequency Response Analysis
Laplace Transforms Important analytical method for solving linear ordinary differential equations. - Application to nonlinear ODEs? Must linearize first.
Laplace Transforms Important analytical method for solving linear ordinary differential equations. - Application to nonlinear ODEs? Must linearize first.
Dynamic Behavior Chapter 5
G1 and G2 are transfer functions and independent of the
UNIVERSITÀ DEGLI STUDI DI SALERNO
Time Response, Stability, and
By: Nafees Ahamad, AP, EECE, Dept. DIT University, Dehradun
Presentation transcript:

Dynamic Behavior Chapter 5 In analyzing process dynamic and process control systems, it is important to know how the process responds to changes in the process inputs. A number of standard types of input changes are widely used for two reasons: Chapter 5 They are representative of the types of changes that occur in plants. They are easy to analyze mathematically.

Step Input A sudden change in a process variable can be approximated by a step change of magnitude, M: Chapter 5 The step change occurs at an arbitrary time denoted as t = 0. Special Case: If M = 1, we have a “unit step change”. We give it the symbol, S(t). Example of a step change: A reactor feedstock is suddenly switched from one supply to another, causing sudden changes in feed concentration, flow, etc.

Example: The heat input to the stirred-tank heating system in Chapter 2 is suddenly changed from 8000 to 10,000 kcal/hr by changing the electrical signal to the heater. Thus, and Chapter 5 Ramp Input Industrial processes often experience “drifting disturbances”, that is, relatively slow changes up or down for some period of time. The rate of change is approximately constant.

Chapter 5 We can approximate a drifting disturbance by a ramp input: Examples of ramp changes: Ramp a setpoint to a new value. Feed composition, heat exchanger fouling, catalyst activity, ambient temperature. Chapter 5 Rectangular Pulse It represents a brief, sudden change in a process variable:

Chapter 5 Examples: Reactor feed is shut off for one hour. URP h Chapter 5 tw Time, t Examples: Reactor feed is shut off for one hour. The fuel gas supply to a furnace is briefly interrupted.

Chapter 5

Other Inputs 4. Sinusoidal Input Chapter 5

Processes are also subject to periodic, or cyclic, disturbances Processes are also subject to periodic, or cyclic, disturbances. They can be approximated by a sinusoidal disturbance: Chapter 5 where: A = amplitude, ω = angular frequency Examples: 24 hour variations in cooling water temperature. 60-Hz electrical noise (in USA) Day night temperature variation (if no weather change)

Chapter 5 Impulse Input Here, It represents a short, transient disturbance. Examples: Electrical noise spike in a thermo-couple reading. Injection of a tracer dye. Chapter 5 Useful for analysis since the response to an impulse input is the inverse of the TF. Thus, Here,

Chapter 5 The corresponding time domain express is: where: Suppose . Then it can be shown that: Consequently, g(t) is called the “impulse response function”.

First-Order System Chapter 5 The standard form for a first-order TF is: where: Chapter 5 Consider the response of this system to a step of magnitude, M: Substitute into (5-16) and rearrange,

Chapter 5 Take L-1 (cf. Table 3.1), Let steady-state value of y(t). From (5-18), t ___ 0 0 0.632 0.865 0.950 0.982 0.993 Chapter 5 Note: Large τ means a slow response.

Chapter 5 For a sine input (1st order process) output is... By partial fraction decomposition,

Chapter 5 Inverting, note: f is not a function of t but of t and w. this term dies out for large t Chapter 5 note: f is not a function of t but of t and w. For large t, y(t) is also sinusoidal, output sine is attenuated by… (fast vs. slow w)

Integrating Process Chapter 5 Not all processes have a steady-state gain. For example, an “integrating process” or “integrator” has the transfer function: Chapter 5 Consider a step change of magnitude M. Then U(s) = M/s and, Thus, y(t) is unbounded and a new steady-state value does not exist.

Chapter 5 Common Physical Example: Consider a liquid storage tank with a pump on the exit line: Assume: Constant cross-sectional area, A. Mass balance: Eq. (1) – Eq. (2), take L, assume steady state initially, For (constant q), Chapter 5

Second-Order Systems Chapter 5 Standard form: which has three model parameters: Chapter 5 Equivalent form:

Chapter 5 Block Notation: Composed of two first order subsystems (G1 and G2) Chapter 5 2nd order ODE model (overdamped) roots:

The type of behavior that occurs depends on the numerical value of damping coefficient, : It is convenient to consider three types of behavior: Damping Coefficient Type of Response Roots of Charact. Polynomial Overdamped Real and ≠ Critically damped Real and = Underdamped Complex conjugates Chapter 5 Note: The characteristic polynomial is the denominator of the transfer function: What about ? It results in an unstable system

Chapter 5 Note: Responses exhibiting oscillation and overshoot (y/KM > 1) are obtained only for values of ζ less than one.

Chapter 5 Note: Large values of ζ yield a sluggish (slow) response. The fastest response without overshoot is obtained for the critically damped case ζ=1. Chapter 5

Several general remarks can be made concerning the responses show in Figs. 5.8 and 5.9: Responses exhibiting oscillation and overshoot (y/KM > 1) are obtained only for values of ζ less than one. Large values of ζ yield a sluggish (slow) response. The fastest response without overshoot is obtained for the critically damped case ζ=1. Chapter 5

Chapter 5

1. Rise Time: tr is the time the process output takes to first reach the new steady-state value. 2. Time to First Peak: tp is the time required for the output to reach its first maximum value. Chapter 5 3. Settling Time: ts is defined as the time required for the process output to reach and remain inside a band whose width is equal to ±5% of the total change in y. The term 95% response time sometimes is used to refer to this case. Also, values of ±1% sometimes are used.

Chapter 5 4. Overshoot: OS = a/b (% overshoot is 100a/b). 5. Period of Oscillation: P is the time between two successive peaks or two successive valleys of the response. 6. Decay Ratio: DR = c/a (where c is the height of the second peak). Chapter 5

Second Order Step Change Overshoot time of first maximum c. decay ratio (successive maxima – not min.) d. period of oscillation Chapter 5

Sinusoidal response Linear second-order system is forced by a sinusoidal input Asin ωt, the output for large value of time (after exponential terms have disappeared) is also sinusoidal signal

The ratio of output to input amplitude is the amplitude ratio AR(= ) The ratio of output to input amplitude is the amplitude ratio AR(= ). When normalized by the process gain (K), it is called normalized amplitude ratio ARN

Chapter 5