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Pressure System Proportional Control Design, Modeling

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Title: Pressure System Proportional Control Design, Modeling


1
-Pressure
System- Proportional Control Design, Modeling
Experiments
  • Cory Richardson
  • Dennis To
  • Jamison Linden
  • 11/15/2009, UTC, ENGR-329

2
Contents
  • Background, Schematics
  • Previous work
  • SSOC, Step Response
  • Sine Response, Bode graphs,
  • Root Locus
  • Proportional Only Controller
  • Proportional Integral Controller
  • Root Locust Model
  • Experimental
  • Conclusions and Recommendations

3
Background - System
                                                
                                                  
                                                  
                             Figure 1. Schematic
diagram of the Dunlap Plant Spray-Paint Booths
4
Background - Block Diagram
                                                
                                                  
                                                 
Figure 2. Block diagram of paint booth system

5
Background - SSOC
Operating Range for Output
Operating Range for Input
6
Transfer Function
m(s) Input
c(s) Output
Transfer Function
7
Feedback Control
8
Background Step Response
9
Background Step Response Results
  • Experimental results
  • K 0.1 0.3 (cm-H2O/)
  • t0 0.5 s
  • t 1.7 s
  • Model results
  • K 0.1 0.3 (cm-H2O/)
  • t0 0.48 s
  • t 1.75 s

10
Frequency Response - Example
T (25.3)
Dc (1.45)
Dm (15)
t (-1.8)
11
Modeling Approach Bode Plots
12
Modeling Approach Bode Plots
13
System
  • 2nd order system
  • fu 0.85 Hz
  • From the model
  • K 0.1 0.35 (cm-H2O/)
  • t0 0.85 s
  • t 1.7 s
  • Kcu 18.2 55.6 (/cm-H2O)

14
Kc Locations 45-60
15
Kc for Different Operating Ranges-based on the
model-
all units are /cm H2O
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Determination of P-only Kcu, fu
  • 45-60
  • Bode 180 /cm-H2O, 0.8 Hz
  • Experimental 180 /cm-H2O, 0.33 Hz
  • 60-75
  • Bode 67 /cm-H2O, 0.8 Hz
  • Experimental 67 /cm-H2O, 0.4 Hz
  • 75-90
  • Bode 42 /cm-H2O, 0.8 Hz
  • Experimental 42 /cm-H2O, 0.42 Hz

29
Dampers were closed for 25 seconds, then opened.
30
Dampers were closed for 25 seconds, then opened.
31
Dampers were closed for 25 seconds, then opened.
32
P-Only Conclusions
  • 45 60 operating range
  • The model ceases to match the system at a Kc
    value of approximately 20.
  • 60 - 75 operating range
  • The model ceases to match the system at a Kc
    value of approximately 14.

33
P-only Conclusions
  • 75 90 operating range
  • The model ceases to match the system at a Kc
    value of approximately 8.

34
System Recommendations (P-only)
35
PI Controller Design Parameter
  • FOPDT Parameter
  • t1.7 sec.
  • To0.8 sec
  • K 0.1-.035 (cm-H20/
  • 2nd Order system
  • FOPDT Parameter to Find
  • Kc
  • ti

36
Root Locus Plots
37
Root Locus
38
Root Locus
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PI Controller
  • Direct Substitution Results
  • Routh Method Results

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Disturbance Response 45-60
Damper closed for 30 seconds then opened for
remainder of experiment
47
Reset Wind-up 45-60 input
48
Conclusion
  • Final FOPDT Parameter
  • Taui3 sec.
  • Kc 8
  • These values will give stable operation
    throughout all ranges
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