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**Dynamic Behavior of Closed-Loop Control Systems**

Chapter 11

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Chapter 11

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Next, we develop a transfer function for each of the five elements in the feedback control loop. For the sake of simplicity, flow rate w1 is assumed to be constant, and the system is initially operating at the nominal steady rate. Process In section 4.1 the approximate dynamic model of a stirred-tank blending system was developed: Chapter 11 where

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Chapter 11

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The symbol denotes the internal set-point composition expressed as an equivalent electrical current signal is related to the actual composition set point by the composition sensor-transmitter gain Km: Chapter 11

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**Chapter 11 Current-to-Pressure (I/P) Transducer Control Valve**

The transducer transfer function merely consists of a steady-state gain KIP: Chapter 11 Control Valve As discussed in Section 9.2, control valves are usually designed so that the flow rate through the valve is a nearly linear function of the signal to the valve actuator. Therefore, a first-order transfer function is an adequate model

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**Chapter 11 Composition Sensor-Transmitter (Analyzer) Controller**

We assume that the dynamic behavior of the composition sensor-transmitter can be approximated by a first-order transfer function, but τm is small so it can be neglected. Controller Suppose that an electronic proportional plus integral controller is used. Chapter 11 where and E(s) are the Laplace transforms of the controller output and the error signal e(t). Kc is dimensionless.

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Chapter 11

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**Chapter 11 1. Summer 2. Comparator 3. Block Blocks in Series**

are equivalent to...

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Chapter 11

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**Chapter 11 “Closed-Loop” Transfer Functions**

Indicate dynamic behavior of the controlled process (i.e., process plus controller, transmitter, valve etc.) Set-point Changes (“Servo Problem”) Assume Ysp 0 and D = 0 (set-point change while disturbance change is zero) Chapter 11 (11-26) Disturbance Changes (“Regulator Problem”) Assume D 0 and Ysp = 0 (constant set-point) (11-29) *Note same denominator for Y/D, Y/Ysp.

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Chapter 11

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Chapter 11

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Chapter 11 Figure Block diagram for level control system.

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Chapter 11

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Chapter 11

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Chapter 11

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**EXAMPLE 1: P.I. control of liquid level**

Block Diagram: Chapter 11

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**Chapter 11 Assumptions 1. q1, varies with time; q2 is constant.**

2. Constant density and x-sectional area of tank, A. (for uncontrolled process) 4. The transmitter and control valve have negligible dynamics (compared with dynamics of tank). 5. Ideal PI controller is used (direct-acting). Chapter 11 For these assumptions, the transfer functions are:

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**Chapter 11 The closed-loop transfer function is: (11-68) Substitute,**

(2) Chapter 11 Simplify, (3) Characteristic Equation: (4) Recall the standard 2nd Order Transfer Function: (5)

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**To place Eqn. (4) in the same form as the denominator of the**

T.F. in Eqn. (5), divide by Kc, KV, KM : Comparing coefficients (5) and (6) gives: Chapter 11 Substitute, For 0 < < 1 , closed-loop response is oscillatory. Thus decreased degree of oscillation by increasing Kc or I (for constant Kv, KM, and A). unusual property of PI control of integrating system better to use P only

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**Stability of Closed-Loop Control Systems**

Chapter 11

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**Chapter 11 Proportional Control of First-Order Process**

Set-point change: Chapter 11

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**Chapter 11 Set-point change = M Offset =**

See Section 11.3 for tank example

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**Chapter 11 Closed-Loop Transfer function approach:**

First-order behavior closed-loop time constant (faster, depends on Kc)

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Chapter 11

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**Chapter 11 General Stability Criterion**

Most industrial processes are stable without feedback control. Thus, they are said to be open-loop stable or self-regulating. An open-loop stable process will return to the original steady state after a transient disturbance (one that is not sustained) occurs. By contrast there are a few processes, such as exothermic chemical reactors, that can be open-loop unstable. Definition of Stability. An unconstrained linear system is said to be stable if the output response is bounded for all bounded inputs. Otherwise it is said to be unstable. Chapter 11

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**Chapter 11 Effect of PID Control on a Disturbance Change**

For a regulator (disturbance change), we want the disturbance effects to attenuate when control is applied. Consider the closed-loop transfer function for proportional control of a third-order system (disturbance change). Chapter 11 is unspecified Kc is the controller function, i.e.,

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Let If Kc = 1, Chapter 11 Since all of the factors are positive, , the step response will be the sum of negative exponentials, but will exhibit oscillation. If Kc = 8, Corresponds to sine wave (undamped), so this case is marginally stable.

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If Kc = 27 Since the sign of the real part of the root is negative, we obtain a positive exponential for the response. Inverse transformation shows how the controller gain affects the roots of the system. Chapter 11 Offset with proportional control (disturbance step-response; D(s) =1/s )

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Therefore, if Kc is made very large, y(t) approaches 0, but does not equal zero. There is some offset with proportional control, and it can be rather large when large values of Kc create instability. Integral Control: Chapter 11 For a unit step load-change and Kc=1, no offset (note 4th order polynomial)

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**Chapter 11 PI Control: no offset**

adjust Kc and I to obtain satisfactory response (roots of equation which is 4th order). Chapter 11 PID Control: (pure PID) No offset, adjust Kc, I , D to obtain satisfactory result (requires solving for roots of 4th order characteristic equation). Analysis of roots of characteristic equation is one way to analyze controller behavior

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Rule of Thumb: Closed-loop response becomes less oscillatory and more stable by decreasing Kc or increasing tI . General Stability Criterion Consider the “characteristic equation,” Note that the left-hand side is merely the denominator of the closed-loop transfer function. Chapter 11 The roots (poles) of the characteristic equation (s - pi) determine the type of response that occurs: Complex roots oscillatory response All real roots no oscillations ***All roots in left half of complex plane = stable system

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Chapter 11 Figure Stability regions in the complex plane for roots of the characteristic equation.

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**Chapter 11 Stability Considerations**

Feedback control can result in oscillatory or even unstable closed-loop responses. Chapter 11 Typical behavior (for different values of controller gain, Kc).

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**Chapter 11 Roots of 1 + GcGvGpGm (Each test is for different**

value of Kc) (Note complex roots always occur in pairs) Figure Contributions of characteristic equation roots to closed-loop response.

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Chapter 11

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**Chapter 11 Routh Stability Criterion Characteristic equation**

(11-93) Where an >0 . According to the Routh criterion, if any of the coefficients a0, a1, …, an-1 are negative or zero, then at least one root of the characteristic equation lies in the RHP, and thus the system is unstable. On the other hand, if all of the coefficients are positive, then one must construct the Routh Array shown below:

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Chapter 11 For stability, all elements in the first column must be positive.

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**Chapter 11 The first two rows of the Routh Array are comprised of the**

coefficients in the characteristic equation. The elements in the remaining rows are calculated from coefficients by using the formulas: (11-94) Chapter 11 (11-95) . (11-96) (11-97) (n+1 rows must be constructed; n = order of the characteristic eqn.)

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**Chapter 11 Application of the Routh Array: Characteristic Eqn is**

We want to know what value of Kc causes instability, I.e., at least one root of the above equation is positive. Using the Routh array, Conditions for Stability The important constraint is Kc<8. Any Kc 8 will cause instability.

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**Figure 11.29 Flowchart for performing a stability analysis.**

Chapter 11

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**Chapter 11 Additional Stability Criteria 1. Bode Stability Criterion**

Ch can handle time delays 2. Nyquist Stability Criterion Ch. 14 Chapter 11

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**Direct Substitution Method**

Imaginary axis is the dividing line between stable and unstable systems. Substitute s = jw into characteristic equation Solve for Kcm and wc (a) one equation for real part (b) one equation for imaginary part Example (cf. Example 11.11) characteristic equation: s + 2Kce-s = 0 (11-101) set s = jw jw + 2Kce-jw = 0 1 + 5jw + 2Kc (cos(w) – j sin(w)) = 0 Chapter 11

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**Chapter 11 Direct Substitution Method (continued)**

Re: 1 + 2Kc cos w = 0 (1) Im: 5w – 2Kc sin w = 0 (2) solve for Kc in (1) and substitute into (2): Chapter 11 Solve for w: wc = rad/min (96.87°/min) from (1) Kcm = 4.25 (vs. 5.5 using Pade approximation in Example 11.11)

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Chapter 11 1 ERT 210/4 Process Control CHAPTER 11 DYNAMIC BEHAVIOR AND STABILITY OF CLOSED-LOOP CONTROL SYSTEMS.

Chapter 11 1 ERT 210/4 Process Control CHAPTER 11 DYNAMIC BEHAVIOR AND STABILITY OF CLOSED-LOOP CONTROL SYSTEMS.

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