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5. Dynamic behavior of First-order and Second-order Systems

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5. Dynamic behavior of First-order and Second-order Systems Contents 1. Standard Process Inputs. 2. Response of First-Order Systems. 3. Response of Integrating Process. – PowerPoint PPT presentation

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Title: 5. Dynamic behavior of First-order and Second-order Systems


1
5. Dynamic behavior of First-order and
Second-order Systems
  • Contents
  • 1. Standard Process Inputs.
  • 2. Response of First-Order Systems.
  • 3. Response of Integrating Process.
  • 4. Response of Second-Order Systems.
  • In this chapter, we learn how process respond to
    typical changes in some of input changes.
  • Two categories in process inputs.
  • 1. Inputs that can be manipulated to control the
    process.
  • 2. Inputs that are not manipulated, classified as
    disturbance or load variable.

2
5.1 Standard Process Inputs
  • - Six important types of input changes.
  • 1. Step input.
  • 2. Ramp input.

Figure 5.1. Step input.
Figure 5.2. Ramp input.
3
3. Rectangular Pulse. or Where
is unit step function. 4. Sinusoidal input.
Figure 5.3. Rectangular Pulse.
4
  • 5. Impulse input.
  • It has the simplest Laplace transform, but it is
    not a realistic input signal. Because to obtain
    an impulse input, it is necessary to inject
    amount of energy or material into a process in an
    infinitesimal length of time.
  • 6. Random inputs.
  • Many process inputs change with time in such a
    complex manner that it is not possible to
    describe them as deterministic functions of time.
    If an input exhibits apparently random
    fluctuation, it is convenient to characterize it
    in statistical terms.

5
5.2 Response of First-Order Systems
  • - General first-order transfer function.
  • Where is the process gain and is the
    time constant.
  • Find and for some particular
    input .
  • 1. Step response.

Figure 5.4. Step response.
6
  • A first-order system dose not respond
    instantaneously to a sudden change in its input
    and that after a time interval equal to the
    process time constant ( ), the process
    response is still only 63.2 complete.
  • Theoretically the process output never reaches
    the new steady-state value it dose approximate
    the new value when t equals 3 to 5
    process time constants.

7
  • 2. Ramp response.
  • Interesting property for large values of time(
    ).
  • After an initial transient period, the ramp
    input yields a ramp output with slope equal to
    , but shifted in time but the process time
    constant .

Figure 5.5. Ramp response. - comparison of input
and output.
8
  • 3. Sinusoidal response.
  • By trigonometric identities.
  • Where .
  • Trigonometric identities.
  • Where .

9
  • Remarks
  • 1. In both (5.21) and (5.22), the exponential
    term goes to zero as leaving a pure
    sinusoidal response.
  • Frequency Response ! (will be discussed later).
  • 2. Since , amplitude is less
    than output f or input . ? Amplitude
    attenuation !

Figure 5.6. Typical sinusoidal response.
10
5.3 Response of Integrating Process Units
  • What is an Integrating Process?
  • The process which has integrating unit( )
    in its transfer function.
  • Open-loop unstable process(Non-self-regulating
    process).
  • A process that cannot reach a new steady state
    when subjected to step changes in inputs is
    called Open-loop unstable process or
    Non-self-regulating process.
  • Which process is an integrating process?

Figure 5.7. Liquid level system with a pump(a) or
valve(b).
11
  • Answer ) (a) is the integrating process!
  • The flowrate of the effluent stream (b) increase
    automatically if the level increase. Therefore,
    the influent flowrate is increased then the level
    will increase and the effluent flowrate also
    increased up to the influent flowrate so the
    level will converge.
  • Liquid level system with a valve is a stable(or
    self-regulating) process.
  • But, in (a), regardless of the level, the
    effluent flowrate is constant due to the pump.
    So, if the influent flowrate is bigger than the
    effluent stream the level always increase, vice
    versa. That is, the difference between the
    influent flowrate and the effluent flowrate is
    integrated to the process output(the level).
  • Liquid level system with a pump is a unstable(or
    non-self-regulating) process.

12
  • Example

Where is independent of .
Integrating process !
Figure 5.8. Liquid level system with a pump.
13
5.4 Response of Second-Order Systems
  • A second order transfer function can arise
    physically,
  • Two first-order processes are connected in
    series.

Figure 5.9. Two first-order systems in series
yield an overall second-order system.
  • A second-order differential equation process
    model is transformed.

14
  • Standard form of the second-order transfer
    function.

15
  • Three important subcases.
  • Denominator of (5.28)
  • Roots
  • unstable second-order system that
    would have an unbounded response to any input.

16
  • 1. Step response.

Case c. , complex root
Underdamped.
Where
17
Figure 5.10. Step response of critically-damped
and overdamped(a), and underdamped(b)
second-order processes.
  • Remarks
  • Responses exhibiting oscillation and overshoot(
    ) are obtained only for values
    of less than one.
  • Large value of yield a sluggish response.
  • The faster response without overshoot is obtained
    for critically damped case( ).

18
  • A number of terms that describe the dynamics of
    underdamped processes.
  • 1. Rise time( ) is the time the process output
    takes to first reach the new steady-state value.
  • 2. Time to first peak( ) is the time required
    for the output to reach its first maximum value.
  • 3. Settling time( ) is defined as the time
    required for the process output reach and remain
    inside a band whose width is equal to
    of the total change in .
  • 4. Overshoot.
  • 5. Decay ratio.
  • 6. Period of Oscillation( ) is the time
    between two successive peaks or two successive
    valleys of the responses.

Figure 5.11. Performance characteristics for the
step response.
19
  • Rise time.
  • Time to first peak.

20
  • Decay ratio.
  • Period of oscillation.

Figure 5.12. Relation between some performance
characteristics of an underdamped second-order
process and the process damping coefficient.
21
  • 2. Sinusoidal response.

As , the first and second terms
vanish. Thus the output for large values of time
is obtained as follows.
Where
  • Amplitude ratio
  • Normalized amplitude ratio

22
  • The maximum value of can be found by
    differentiating (5.45) with respect to .

For , there is no maximum.
  • At high frequency, the output is well damped.
  • At low frequency, the output is not damped well.

Figure 5.13. Sinusoidal response amplitude of a
second-order system after exponential terms have
become negligible.
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