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بسم الله الرحمن الرحيم Advanced Control Lecture two Mohammad Ali Fanaei Dept. of Chemical Engineering Ferdowsi University of Mashhad Reference: Smith & Corripio, “Principles and practice of automatic process control, 3 rd ed., Wiley, 2006
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Empirical Modeling (Step Testing) Final Control Element Process Sensor/ Transmitter Step Change Record m(t)m(t)c(t) Process Gain:
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FOPDT Model Fit 1 :
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FOPDT Model Fit 2 :
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FOPDT Model Fit 3 :
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Control Valve Control Valve Action Control Valve Characteristics Control valve Capacity m(t)m(t)vp(t)Cv(t)Cv(t)f(t)f(t)
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Control Valve 1.Control Valve Action Fail-Closed (FC) or Air-to-Open (AO) : Fail-Open (FO) or Air-to-Close (AC) :
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Control Valve 2.Control Valve Characteristics Linear Quick-opening Equal percentage Rangeability parameter
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Control Valve 3.Control Valve Capacity The flow in U.S. gallons per minute (gpm) of water that flows through a valve at a pressure drop of 1 psi across the valve Liquid Flow: gpm psi Gas Flow: scfh Critical flow factor (0.6-0.95) Inlet pressure psia Inlet temperature o R Where
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PID Control 1.Action of Controller If the action is not correctly selected, the controller will not control Reverse action (increase/decrease)
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PID Control Direct action (increase/increase) To determine the action of a controller, the engineer must know: 1.The process requirement for control 2.The fail-safe action of the control valve
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PID Control 2.Type of PID Controller Ideal PID: Parallel PID: Series PID: Range 0.05 to 0.2
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PID Control 3.Reset Windup
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PID Control 4.Reset Feedback (RFB) Internal Reset Feedback
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PID Control 4.Reset Feedback (RFB)
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PID Control 4.Reset Feedback (RFB) External Reset Feedback
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PID Control 5.Back Calculation Back-Calculation with internal tracking Tracking Time Constant T d < T t < T i
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PID Control 5.Back Calculation Back-Calculation with external tracking External tracking signal
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PID Control 5.Proportional and Derivative Kick Proportional KickDerivative Kick Range: 0-1Range: 0-1, Commonly zero Two Degrees of Freedom or ISA - PID
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PID Control
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