Lecture 29 Margins: Bode, Nyquist
Process Control
- Prof. Kannan M. Moudgalya
IIT Bombay Monday, 14 October 2013
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Lecture 29 Margins: Bode, Nyquist Process Control Prof. Kannan M. - - PowerPoint PPT Presentation
Lecture 29 Margins: Bode, Nyquist Process Control Prof. Kannan M. Moudgalya IIT Bombay Monday, 14 October 2013 1/27 Process Control Margins Outline 1. One more Nyquist plot example 2. Recalling margins from Bode plot 3. Margins using
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◮ G(s) is open loop transfer function ◮ Does not have poles and zeros on RHP ◮ Put in a closed loop with a proportional
◮ As Kc increases, closed loop system
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G1 (dB)
1 10 10 20 15 10 5
10 10
Bode plot
10 10 10 10
1 Phase
When Kc is increased to 4 ωpc Gain Margin = 4 = 12dB
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◮ Locate ωc, where ∠G(jωc) = −180◦ ◮ Find |G(jωc)| at that point ◮ Can increase gain of the system by Kc
◮ Can verify that we can increase Kc until 4 ◮ This method was followed in the previous
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G1 (dB)
1
10 10 20 15 10 5
10 10
Bode plot Phase
1
10
10
10 10
Phase Margin = 56.8 deg ωgc
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◮ When φ(ωg) = −123.2◦, |G(jωg)| = 1 ◮ ωg = 1.57 radians ◮ The phase can drop by 56.8◦ for the
◮ The phase margin is 56.8◦ ◮ Call this ω as ωgc or ωg
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◮ C1 contour covers RHP in the s-plane ◮ C2 contour is a plot of 1 + KcG(s)
◮ C3 is C2 − 1 ◮ Stability in terms of C3 contour:
◮ For stability, C3 contour should encircle −1
◮ P is the number of open loop unstable poles
◮ If P = 0, stability condition is, N = 0
◮ We will consider only systems with P = 0
◮ So we demand no encirclement of (−1, 0)
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R2
Im(G(s)) Re(G(s)) C41 C43 (−0.5, 0) at ω = √ 11 (5, 0) At ω = 1, (0, −3)
R1 R3 R4
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α Re(G) Im(G)
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φ Re(G) Im(G)
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◮ Have to use GM and PM together ◮ One alone is insufficient ◮ Examples ◮ Modulus/vector margin
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◮ Margins ◮ Relation between Nyquist and Bode plots
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