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FLOW RATE CONTROL SYSTEM
SECOND ORDER PLUS DEAD TIME MODEL April 20, 2006 U.T.C Engineering 329
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Yellow Team Jimy George Jeff Lawrence Taylor Murphy Jennifer Potter
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Outline Flow System Background SOPDT System Theory Model Results
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Outline Proportional Controller Comparison of FOPDT & SOPDT results
Conclusion
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Flow System Setup
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Block Diagram
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Laplace Domain R(s) C(s)
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Time Domain
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Modeling Observations
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Parameters involved
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Modeling Observations Recap
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Negative Feedback Loop
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Closed Loop Transfer Function
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Characteristic Equation
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Characteristic Equation
For
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Solving CE for Kc Direct Substitution Set s = iωU
Set like terms equal to zero Imaginary part: [ ωU3-( Kcu) ωU]i=0i
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Direct Substitution (cont’d)
Real part: 0.24Kcu ωU2 + 1 = 0 ωU = 5 => fu = 0.8 Kcu = 8.3 %/(lb/min)
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Corresponding Frequency Experiment
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Observations Phase Angle = -1800 Amplitude Ratio = 0.12
Kcu calculated = 8.3
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Comparison of fu
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Comparison of Kc
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Conclusion Kc = 8.3 %/(lb/min) SOPDT more accurate than FOPDT
Always scope for improved results
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