
2021.05.26 REV. DUALVALVE PRESSURE CONTROLLER OPERATING MANUAL 13
Establishing Setpoint Limits
CONTROL →Setpoint Setup →Setpoint Limits
The setpoint limits menu configures upper and lower limits for selecting a pressure control setpoint. By default, the controller
will only be limited by its measuring range; however, more strict limits may be beneficial in certain critical applications.
Over a serial connection, requesting a setpoint outside the limit will be rejected and an error will be returned. When
using an analog setpoint signal, setpoints that are outside of the setpoint limits are treated as if they were at the nearest
limit. For example, if you request a setpoint that is below the lower limit, the controller sets the setpoint at the lower limit.
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Note: When changing from one control loop variable to another, the pressure controller remembers setpoint limits as
percentages of full scale. For example, a 15- limit on a 30- pressure controller (50% of full scale) will become a
limit of 50% if the control loop is changed to valve drive.
Control Loop
Changing the Controlled Variable
CONTROL →Control Loop →Control
Selectable control loop variables include pressure (absolute, gauge, or dierential) and valve drive.
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Note: Pressure controllers with upstream valves will control the outlet pressure. Those with downstream valves can control
upstream backpressure, but these must be configured for this type of control.
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Warning: When changing the control loop, you may need to adjust the PID settings for optimal stability and speed of
response.
Adjusting the PD/PDF or PDI Control Algorithms
CONTROL →Control Loop →Loop Type
Your pressure controller uses an electronic closed loop controller to determine how to actuate its valve(s) in order to
achieve the commanded setpoint. These settings are tuned for your specific operating conditions, but changes to your
process sometimes require on-site adjustments to maintain optimal control performance. If you encounter issues with
control stability, oscillation, or speed of response, fine-tuning your closed loop control may help.
For most applications, the PD/PDF algorithm is recommended.
Tuning the PD/PDF Control Algorithm
The controller’s default control algorithm (PD) employs pseudo-derivative feedback (PDF) control, which uses two editable
variables:
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The larger the Dgain, the slower the controller will correct errors between the commanded setpoint and the measured
process value. This is equivalent to the P variable in common PDF controllers.
• The larger the Pgain, the faster the controller will correct for osets based on the size of the errors and the amount
of time they have occurred. This is equivalent to the I variable in common PDF controllers.
✓ Note: The D and P variables in the PD/PDF control algorithm are more typically referred to as P and I, respectively, in PDF
controllers.
Tuning the PDI Control Algorithm
The controller’s PD²I control algorithm (also called PDDI) is used to provide faster response, most commonly in dual-valve
flow and pressure controllers. This algorithm uses typical PI terms and adds a squared derivative term (D):
• The larger the Pgain, the more aggressively the controller will correct for errors between the commanded setpoint
and the measured process value.
• The larger the Igain, the faster the controller will correct for osets based on the size of the errors and the amount
of time they have occurred.
• The larger the Dgain, the faster the controller will predict necessary future corrections based on the current rate of
change in the system. This often results in slowing the system down to minimize overshoot and oscillations.