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Pid sp tracking

With setpoint tracking in the controller, for the entire time the controller is in manual mode, the SP value of the controller will be held equal to the PV value (whatever that value happens to be). Once the operator decides that switching the controller to automatic mode is appropriate, the SP value freezes at the last PV manual mode value, and the controller will continue to control the PV at that SP value. Ideally, the scale and units of the master OP should be the same as the PV and SP of the slave loop. That allows direct transfer and tracking without scaling.

Unlike later cartridges, the SP1 and 2 (the difference being that SP1 cartridges had a half inch mounting bracket for use in non B&O arms) could be specified with a number of different styluses suitable for various roles.

When you do so, use the Plant menu in PID Tuner to specify your plant model. Examine the reference tracking rise time and settling time. Right-click on the plot and select Characteristics > Rise Time to mark the rise time as a blue dot on the plot. Select Characteristics > Settling Time to mark the settling time.

The Dependent, Ideal PID Form A popular way vendors express the dependent, ideal PID controller is: Where: CO = controller output signal (the wire out) CO bias = controller bias; set by bumpless transfer e(t) = current controller error, defined as SP – PV SP = set point PV = measured process variable (the wire in) Kc = controller gain, a tuning parameter PID = Proportional, Integral, Derivative algorithm. This is not a P&ID, which is a Piping (or Process) and Instrumentation Diagram. PV = Process Variable – a quantity used as a feedback, typically measured by an instrument. Also sometimes called “MV” – Measured Value.

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Main reason to use setpoint tracking is to minimize a bump in control: if someone places the controller in Manual mode, the target Setpoint (SP) will track, or follow, the Process Value (PV). So, in Manual mode, the controller output might be 40% with a PV of 238 kPathe SP will also be 238 kPa. 4.3.2.2 Setpoint Tracking. A second component of bumpless transfer is to have the setpoint track the process variable.