Dynaflow, User manual - operation, Alternate pid equation – Ransburg DynaFlow User Manual User Manual

Page 63: Pid tuning methods - standard pid

Advertising
background image

LN-9400-00.9

DynaFlow

TM

User Manual - Operation

59

pressure. This is due to the Integral term of the

PID control. If the restriction causing the low

flow condition is removed suddenly while a large

control output signal exist, then a relatively long

amount of time is required for the Integral term

of the PID to reduce the control output back to a

normal range since the Integral term is proportional

to time and also due to the inherent response of

the system. If fluid flow response has changed

significantly with the same setup that previously

produced good response, then inspect the system

for component failure, blockages, and check the

fluid type and viscosity.

Alternate PID Equation

The normal PID equation is based on the error

between the desired set point and the actual flow

rate for the CHANNEL. If the set point is varied

dynamically by a PLC via RIO or by a robot via

Analog Input, it may be desirable to implement

an alternate form of the equation. The alternate

form of the equation uses the set point for the

proportional term of the equation. The Integral

and Derivative terms are the same, but slightly

different scale factors are used.

To enable the alternate PID equation, turn on DIP

SW1-4 (or SW1-8) on the Channel Module for

each CHANNEL of the GUN.

PID Tuning Methods - Standard

PID

1. Select the nominal flow rate for the GUN.

2. Set Kp and Kd parameters to zero. Do this

for both CHANNELS if this is a two-component

GUN.

3. Set Ki for the Slave CHANNEL to zero (as-

suming this is a two-component GUN).

4. Set Ki for the Master CHANNEL to the de-

fault value shown in "Default Control Parameters"

chart and "Typical Ranges for Control Parameters"

chart in this section.

5. Cycle the GUN from READY to RUN so the

new parameters are sent to the Channel

Module(s).

6. Trigger the GUN. If the flow rate does not

oscillate, or the oscillations decrease in amplitude

in a few seconds, increase Ki by 100 and repeat

from step 5. If the flow rate oscillates with increas-

ing amplitude, decrease Ki by 50 and repeat from

step 5. 8If the flow rate oscillates with a constant

amplitude, proceed to step 7.

7. Set Ki to one-half the present value.

8. Set Kp to the default value shown in the "Default

Control Parameters chart" and Typical Ranges for

Control Parameters chart" in this section.

9. Cycle the GUN from READY to RUN so the

new parameters are sent to the Channel Mod-

ule(s).

10. Trigger the GUN. If the flow rate does not

oscillate, or the oscillations decrease in amplitude

in a few seconds, increase Kp by 30 and repeat

from step 9. If the flow rate oscillates with increas-

ing amplitude, decrease Kp by 15 and repeat from

step 9. If the flow rate oscillates with a constant

amplitude, proceed to step 11.

11. Set Kp to one-third the present value.

12. Cycle the GUN from READY to RUN so the

new parameters are sent to the Channel

Module(s).

13. Trigger the GUN. If the flow rate does not

oscillate, proceed to step 14. If the flow rate is

oscillating, reduce Ki by 50 and/or reduce Kp by

15 and repeat from step 12.

14. At this point, the tuning procedure is completed

for most flow control applications. However, if

there is a great amount of lag

time from

the point of sensing the flow rate to where the

material volume regulator is located, the derivative

term of the PID equation may be required. In that

case, set Kd to the default value shown in "Default

Control Parameters" chart and "Typical Ranges

for Control Parameters" chart in this section.

15. Cycle the GUN from READY to RUN so the

new parameters are sent to the Channel

Module(s).

Advertising