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Commentaria in Aristotelem graeca, voluminis XXIII - Calaméo

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Instruktion A B C D E F G H I J K L M N O P Q R S T U V W X Y

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Pid sp pv cv

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The temperature indicating controller (TIC) compares a process variable (PV) value to a setpoint (SP) value, and calculates and sends an output (OP) signal to the steam flow control valve. The process data associated with the tank temperature control loop in a data historian would include: PV or MV. The process variable or measured variable. This function toddles betwee the E=SP-PV (Setpoint-Process Varable) and E=PV-SP. E=PV-SP is direct acting and causes the output Control Variable CV to increase when the input Process Varaiable PV is larger than the Setpoint.

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High AlarmLow AlarmComm. Err. FF Disturbance must be known and modeled explicitly.

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Pid sp pv cv

PV = Process Variable. P = Proportional Control. I = Integral Control. (CV). INSTALLED CHARCTERISTICS FOR QUICK OPENING CONTROL VALVE SP. PV. Disturbance applied 40.

I was playing with the block. When SP>PV, with the tuning parameter that I used yesterday, the CV is ramping up slowly.. which is what i wanted however, when PV>SP, the CV is still ramping up whenit should be ramping down.. I didnt know that programming a PID block can bethis difficult!!
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LCCC Workshop on Process Control Johnsson, Charlotta - LU

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