Digital Tuning Flashcards
What tuning parameters would you use for flow of liquid and gas?
- P
- PI
- PID
- Adaptive
- Feedforward
Liquid> PI
Gas> PI
What tuning parameters would you use for pressure control of liquids, gases, and vapour?
- P
- PI
- PID
- Adaptive
- Feedforward
Gas> P
Liquids> P or PI
Vapour> PID or Feed Forward Control
What tuning parameters would you use for level control of liquid in Surge and Tight Control
- P
- PI
- PID
- Adaptive
- Feedforward
Tight control 5% to 10%> P or PI
Surge> P or PI
What tuning parameters would you use for Temperature
- P
- PI
- PID
- Adaptive
- Feedforward
Temp> PID or Feedforward Control
What tuning parameter would you use for Composition Control
- P
- PI
- PID
- Feedforward
- Adaptive
PID, Adaptive, Feedforward
When calculating tuning settings for a PID controller what happens if Td is less then .1 min?
Redo calculations as a PI controller, b/c controller is fast enough already
How does the interactive PID algorithm work?
Proportional effects Derivative, and both effect Integral
How does Standard PID algorithm work?
Most tuning rules are based on this algorithm
Proportional effects both Derivative and Integral, but Derivative and Integral don’t effect each other.
How does Parallel algorithm work?
Parallel removes any interaction between all three actions.
If load disturbances significantly affects the Non-Linear control loop what are three possible solutions and how do they work?
- Detune loop: tune loop for steepest slope, where its loop gain is highest. At all other points control will be slow
- Multipoint characterizer: find actual results versus entered and compensate.
- Adaptive control: cut graph in half, find loop gain for them and enter them in for desired regions.
True or False: Equal % valve linearizes control loop for load disturbances and SP changes
False.
Linearizes load changes, non-linear for SP changes
List 3 components that cause non-linearity in a control loop.
Hint: 3 components of a control loop
- TX
- Process
- FCE
How does Parallel algorithm work?
Parallel removes any interaction between all three actions.
If load disturbances significantly affects the Non-Linear control loop what are three possible solutions and how do they work?
- Detune loop: tune loop for steepest slope, where its loop gain is highest. At all other points control will be slow
- Multipoint characterizer: find actual results versus entered and compensate.
- Adaptive control: cut graph in half, find loop gain for them and enter them in for desired regions.
True or False: Equal % valve linearizes control loop for load disturbances and SP changes
False.
Linearizes load changes, non-linear for SP changes