• IPD operations are conducted as follows.
Item
Deviation (DVn)
Output variation (MV)
Bn
Kp: Gain
Ti: Integral time
Td: Derivative time
Md: Derivative gain
CT: Control cycle
DVn: Deviation
DVn-1: Last deviation value
PVn: Process variable
PVn-1: Last process variable
PVn-2: Process variable before the last value
SVn: Engineering value conversion processing result
The integral term and derivative term are as follows under the following conditions.
Item
Condition
Derivative
When Td = 0
term
When the control mode is MAN
When the control mode is CMV
Integral
When Ti = 0
term
When either of MH or ML error has occurred, MVP > MH and the
following expression is satisfied
CT
×DVn>0
Ti
• When either of MH or ML error has occurred, MVP < ML and the
following expression is satisfied
CT
×DVn<0
Ti
Ti: Integral time
CT: Control cycle
DVn: Deviation
MH: Output high limit value
ML: Output low limit value
MVP: MV Internal operation value
Set an integral multiple of the execution cycle (T) as a control cycle (CT).
Set 0.0 or a value equal to or larger than the control cycle (CT) as an integral constant.
PID operations of this tag access FB are performed every control cycle (CT) (MV output).
In other execution cycles (T), the last value is held (MV = 0).
Direct action
DVn = PVn - SVn
CT
ΔMV = Kp × {
× DV
+ (PV
- PV
n
n
Ti
Gain
Integral
Proportional Derivative
Md×Td
×
B
=B
+
n
n-1
Md×CT+Td
CT×B
{(PV
-2PV
+PV
)-
n
n-1
n-2
Td
10.15 I-PD Control (Enable Tracking for primary loop) (M+P_IPD_T)
Reverse action
DVn = SVn - PVn
CT
) + B
}
ΔMV = Kp × {
n - 1
n
Ti
Gain
Integral
Md×Td
B
=B
+
n
n-1
Md×CT+Td
n-1
{-(PV
-2PV
}
n
Processing
Bn = 0
CT
×DV
=0
n
Ti
10 LOOP CONTROL OPERATION
× DV
- (PV
- PV
) + B
}
n
n
n - 1
n
Proportional Derivative
×
CT×B
n-1
+PV
)-
}
n-1
n-2
Td
273
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