
2021.05.26 REV. PRESSURE CONTROLLER OPERATING MANUAL 13
Power-Up Setpoint with Ramping
CONTROL →Setpoint Setup →Power Up Setpoint →Ramp
Any setpoint ramp will always start from zero on power-up. Similar to the zero setpoint option
(page 12), the device can either honor the ramp rate (Honor from 0) or jump to setpoint
(Jump from 0) as quickly as possible.
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.
✓
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-PSIG 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.
✓ 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.
! 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 were tuned
for your specific operating conditions, but changes to your process sometimes require on-site
adjustments to maintain optimal control performance. Fine-tuning your closed loop control
may help issues with control stability, oscillation, or speed of response.
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:
•
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 Pvariable 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 Ivariable
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.
Setting a minimum setpoint.
The setpoint limits menu.
The control loop menu in PD/PDF
control mode.
Setting a P Gain.