
2021.05.26 REV. LIQUID FLOW CONTROLLER OPERATING MANUAL 13
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.
!
Warning: Flow controllers that have non-zero lower setpoint limits cannot be set to stop flow until the lower limit has been
cleared.
✓
Note: When changing from one control loop variable to another, the flow controller remembers setpoint limits as percentages
of full scale. For example, a 1-LPM limit on an LCR-2LPM controller (50% of full scale) will become a limit of 50 (50%
of 100 ) if the control loop is changed to gauge pressure.
Control Loop
Changing the Controlled Variable
CONTROL →Control Loop →Control
The controller can control the flow rate or the pressure in your process. Selectable control loop variables include volumetric
flow, gauge pressure, and valve drive.
✓ Note: When pressure is selected as the control loop variable, flow 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 from volumetric flow to gauge pressure, 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 liquid flow 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. 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:
•
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
traditional PDF controllers.
Tuning the PDI Control Alogrithm
The controller’s PDI 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 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 needed 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.