Control Theory - Control-Intro PPT

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  • 7/29/2019 Control Theory - Control-Intro PPT

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Open Loop

    Plant Characteristics

    Linearity

    Linear or State variable repr.

    State variable repr.

    Transfer Function (observable & controllable part): Y(s)/U(s)

    Non Linear

    State Variable repr.

    Linear Approximation (Linerarization at operational points,

    Describing Function, etc)

    PlantU(t) Y(t)

    X AX BU Y CX DU= + = +

    ( , ) ( , )X f X U Y g X U= =

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Time

    Time Invariance (fixed coefficients)

    Time Variance (dynamic coefficients)

    Granularity

    lumped parameters (linear differential equations) distributed parameters (partial differential equations)

    Number of Inputs and Outputs

    SISO, SIMO, MISO, MIMO

    ( ( ), ( ), ) ( ( ), ( ), )X f X t U t t Y g X t U t t= =

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Closed Loop (Output feedback)

    Bang-Bang Control

    E = SP - YU = Sign(E) orU = Sign(E+/- 1/2gap)

    gap

    Issues:

    Limit Cycles and Overshooting

    Gap reduces cycling frequency

    PlantU(t) Y(t)ControllerSP+

    -

    E

    E

    U

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Closed Loop (Output feedback)

    Proportional Control

    KP = Proportional Gain (to control rise time)

    M = Manual reset

    Issues: Offset Error (SSE)

    E = SP - Y

    U K E M P= +

    PlantU(t) Y(t)ControllerSP+

    -

    E

    E

    M

    UKP

    1

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Closed Loop (Output feedback)

    Proportional Integral (PI) Control

    E = SP - YEdtKEKU IP +=

    KP = Proportional Gain (to control rise time)KI = Integral Gain (to control SSE)

    M = Manual reset

    Issues: Slow in correcting SSE

    PlantU(t) Y(t)ControllerSP+

    -

    E

    E

    U

    E ControlSurface

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    Closed Loop (Output feedback)

    PlantU(t) Y(t)ControllerSP+

    -

    E

    Proportional Integral Derivative (PID) Control

    E = SP - Y

    dt

    dEKEdtKEKU DIP ++=

    KP = Proportional Gain (to control rise time)KI = Integral Gain (to control SSE)

    KD = Derivate Gain (to anticipate error)

    Issues: Pure Derivative term not realizable (non-causal)

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    Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved

    Control Theor

    dt

    dEKEdtKEKU DIP ++=

    Issues: Pure Derivative term not realizable (non-causal)

    Usually solved by placing a pole with large negative value (-A):

    U s

    E sK

    T sT s

    KT s

    Ts

    s A

    I

    D

    I

    D

    ( )

    ( )( )

    ( )

    = + +

    + ++

    11

    11