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07/20/2005
Note :
* typical range of setting
P: control valve should have positioner
ER: external reset is recommended
Po or Ve: the digital algorithm used should be the positional or velocity type
SOME COMMENTS in addition to the figures given in the tabulation below:
Harold Wade, Wade Associates, Inc. Hlwade@aol.com
|
CONTROLLED VARIABLES |
PB (%) |
I (minutes/repeat) |
D (Minutes) |
OTHER (See Note) |
|
Level, Surge Drum |
(HLA-LLA)-!0% |
Not req’d |
Not req’d |
|
|
Level, Tight Cont |
40% - 200% |
1.5 – 15 |
Not req’d |
P |
|
Flow |
100 – 250% |
0.2 – 1.0 |
Never |
|
|
Pressure, Gas |
2% - 5% |
May not be req’d |
Not req’d |
|
|
Pressure, Boilr Mstr or Dist Tower |
10% - 50% |
3.0 – 10.0 |
0.0 – 1.0 |
P (if not a cascade master) |
|
Temperature (std.) |
10 – 50% |
5.0 – 20.0 |
0.0 – 2.5 |
P |
|
Cascade Master |
10 – 50% |
5.0 – 20.0 |
0.0 – 2.5 |
ER |
|
Cascade slave |
50% - 200% |
2.0 – 5.0 |
CW Cont on Exoth Reactor: 0.5 – 1.0 Otherwise: Not req |
P |
|
pH |
100 – 1000% |
3.0 – 20.0 |
0.5 – 2.0 |
P (also linearize PV) |
BE CAREFUL ABOUT general rules for specific PID numbers because there are different algorithms available. In general, use positioners on all the loops. Positioners may be overkill on fast pressure loops. Use External Reset on inner (slave) loops of cascades or if there are limiters or selectors on the other loops. Velocity or positional algorithms will work; however there are often two distinct advantages to positional algorithms: fewer numerical problems and better anti-reset windup. If you use a controller from any of the major DCS vendors, you will be fine.
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