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CHE 185 – PROCESS CONTROL AND DYNAMICS

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CHE 185 – PROCESS CONTROL AND DYNAMICS. WORKSHOP 2. P-only control of tank level. OBJECTIVES: 1. Understand the concept of closed loop feedback control (in contrast to open loop). 2. See the effects of controller gain on its performance (Define performance) . P-only control of tank level.

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p only control of tank level
P-only control of tank level
  • OBJECTIVES:
    • 1. Understand the concept of closed loop feedback control (in contrast to open loop).
    • 2. See the effects of controller gain on its performance (Define performance)

.

p only control of tank level1
P-only control of tank level
  • OBJECTIVES:
    • 3. Realize the difference between set point tracking and disturbance rejection controls (show response curves for each)
    • 4. Predict the steady state error of the P-only control, and understand the existence of it for P-only control
p only control of tank level2
P-only control of tank level
  • OBJECTIVES:
    • 5. Understand what proportional band is.
  • overall objective is to maintain inventory; tank-filling operation is to maintain constant level; transmitter, control valve, and controller are the devices to achieve that objective.
typical results
TYPICAL RESULTS
  • Fit a FOPDT dynamic model to the CO to PV (cause and effect) step test data CO = controller output; PV = measured process variable (level in the tank)
typical results1
TYPICAL RESULTS
  • Fit a FOPDT dynamic model to the CO to PV
typical results2
TYPICAL RESULTS
  • 60%  68% step in Controller Output
typical results3
TYPICAL RESULTS
  • 60%  68% step in Controller Output
typical results4
TYPICAL RESULTS
  • 60%  68% step in Controller Output
typical results5
TYPICAL RESULTS
  • ACTIVATING THE CONTROLLER - Click the level controller icon (LC), switch from Manual Mode to PID, enter your SP, CObias and Kc values. Switch integral to ‘off: Integral Mode’. Derivative Mode should also be off.
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