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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 1 / 7Applied Sciences

    Name:............................

    Formulas:

    Laplace Transform Table:

    ( )t 1

    s

    e a t 1

    s a

    t 12

    s

    1

    1a

    e at

    1

    s s a

    sin at as a

    2 2

    cos at ss a

    2 2

    for d1: 11 2

    2,1

    21

    2

    21

    1 21

    ddTTwhereeTT

    TeTT

    T Tt

    T

    t

    1

    2 12 2( )T s d T s s

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 2 / 7Applied Sciences

    Problem 1: (6 points)

    Given a system with input signal x(t) and output signal y(t) which is described by

    xTyTy

    a) Obtain the transfer function G s Y s

    X s( )

    ( )

    ( ) .

    b) The input is x(t)=(t). What is the Laplace-transform of x(t) ? What is the Laplace-transform of y(t) ? Obtain y(t).

    c) Make a sketch of the Nyquist plot of G(s).The starting point and the end point must be clearly shown.

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 3 / 7Applied Sciences

    Problem 2: (7 points)

    Given a system which is the series connection of an integrator (transfer func-

    tion: 1

    T si

    ) and a lowpass-system (transfer function:

    sT1

    1).

    a) Make a sketch of the Nyquist plot for T=Ti=1s.Rough sketch is sufficient; the starting point and the end point must be clearlyshown.

    b) Obtain the step response (as a formula) of the system for Ti= T.

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 4 / 7Applied Sciences

    Problem 3: (10 points)

    Given the following control loop. Theprocess is described by

    TsTsK

    sG

    1

    )( .

    a) Obtain the transfer function G(s) = C(s)/R(s) of the closed loop, if a P-controllerwith gain V is used.

    b) What is the steady state error (in %) for K=4, V=1 and T=1s ?

    c) Is it possible, that the control loop is unstable with P-control ? Why ?

    d) If the strategy of cancelling poles is to be used, which controller is to be used(P, PI, PD, PID or I).? Why?

    controller process

    -

    r ce y

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 5 / 7Applied Sciences

    Problem 4: (7 points)

    Given the following Nyquist plot of anopen control loop. A P-controller withgain 1 is used.

    a) What is the order of the process?

    b) What is the maximum gain of thecontroller, so that the control loop is

    still stable.Approximate value issufficient; explain the way how theresult is obtained.

    c) What is the steady state error (in %)?

    -2 -1 0 1 2 3 4 5-5

    -4

    -3

    -2

    -1

    0

    1

    real part

    imaginarypart

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 6 / 7Applied Sciences

    Problem 5: (9 points)

    A process defined by sTwithe

    Ts

    G sT

    process 11

    is controlled by a P-Controller (gain

    V).

    a) Draw the block diagram for the closed loop.

    b) Make a sketch of the Nyquist plot of the open loop for V=1.

    c) What is the maximum value for V for which the control loop is still stable?

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    Prof. Dr.-Ing. F. Keller Control Theory CSexss12.docKarlsruhe University of Examination Summer 2012 page 7 / 7Applied Sciences

    Problem 6: (9 points)

    We consider a liquid level control system. The liquid level h (dimension: m) in a con-tainer is to be controlled. The cross section area of the container is A. The controlleroutput is q

    controller(flow rate, dimension: m

    3/s).

    a) What is the transfer function of the process (input: qcontroller, output: h)

    b) We use a P-controller with gain K. Obtain the transfer function of the closed loop.Is it possible that the control loop is unstable? Why?

    c) Make a drawing of the following signals: reference input, controller output, con-trolled variable if the container is empty for t=0. The reference input is a step from

    0 to 1m. Parameters:m

    s

    m

    KmA

    3

    2

    1

    ,1