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CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 1
Chapter 6
Dynamic Behavior of Higher-order
and Time delay Processes
6/30/2014
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Chapter Objectives
At the end of this chapter, you will be able to
Explain Interacting and non-interacting systems
Derive transfer functions for higher order systems
Explain delay times in processes
Develop transfer functions for delay times
Develop approximate expressions for delay times
6/30/2014 CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 2
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Interacting and Noninteracting
Processes
Processes with variables that interact with each other, or
that contain internal feedback of material or energy
will exhibit interacting behavior
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 36/30/2014
Ch
apte
r 6
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Non-interacting Processes
The two-storage tanks were connected in series in such a way that liquid level in the
second tank did not influence the level in the
first tank.
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 46/30/2014
The following transfer functions were derived:
1)(
)(
1
11
s
K
sQ
sH
i (6.1)
11
1 1
)(
)(
KsH
sQ
(6.2)
1)(
)(
2
2
1
2
s
K
sQ
sH
(6.3)
22
2 1
)(
)(
KsH
sQ
(6.4)
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Non-interacting Processes
Tank 2 level h2 is related to qi by a second-ordertransfer function that can be obtained by simplemultiplication
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 56/30/2014
11)()(
)(
)(
)(
)(
)(
)(
21
21
1
1
1
22
ss
K
sQ
sH
sH
sQ
sQ
sH
sQ
sH
ii (6.5)
A simple generalization of the dynamic
expression in (6.5) is applicable to n tanks in
series
n
i
i
n
i
n
s
K
sQ
sH
1
1)(
)(
n
i
ii
n
ssQ
sQ
1
1
1
)(
)(
(6.6)
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An interacting process
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 66/30/2014
In the process shown above, h1 depends on h2as a result of interconnecting stream with flow
rate q1.
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An interacting process
The equation for flow from Tank 1 to Tank 2 must
be written to reflect that physical feature.
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 76/30/2014
)(1
21
1
1 hhR
q (6.7)
For Tank 1, the level transfer function can be
derived as
1
1
)(
)(
121122
2
2121
21
22121
1
sARARARsAARR
sRR
ARRRR
sQ
sH
i
(6.8)
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An interacting process
Consequently, the overall transfer function
between h2 and qi is
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 86/30/2014
12)(
)(22
22
ss
R
sQ
sH
i (6.10)
The transfer function relating h1 and h2 is
1)(
)(
21
221
21
2
1
2
sRR
ARR
RR
R
sH
sH (6.9)
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Processes with Time Delays
Time delays occur due to:
1.Fluid flow in a pipe
2.Transport of solid material (e.g., conveyor belt)
3.Chemical analysis
- Sampling line delay
- Time required to do the analysis (e.g., on-line
gas chromatograph)
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 96/30/2014
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Processes with Time Delays
If a fluid is transported through a pipe in plug flow,
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 106/30/2014
flowrate volumetric
pipe of volume
velocityfluid
pipe oflength (6.11)
Point 1 Point 2
Transportation time between points 1 and 2 is given by
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Processes with Time Delays
( )( )
( )
s Y sG s eU s
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 116/30/2014
0 for (6-27)
for
ty t
u t t
(6.12)
Suppose that x is some fluid property at point 1, such as concentration, and y is the same property at point 2 and that both x and y are deviation variables. Then
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Processes with Time Delays
The output y(t) is simply the same input function shifted backward in time by the
amount of the delay translation in time.
The transfer function of a time delay of magnitude is given by
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 126/30/2014
(6.13) sesG
sX
sY )()(
)(
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Processes with Time Delays
Polynomial approximations to (non-rational function)
Taylor series expansion:
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 136/30/2014
...!5
!4
!3
!2
1
55443322
ssssse s
(6.14)
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Processes with Time Delays
Pad approximation (A ratio of two polynomials)
1/1 Pad approximation
Performing the long division in (6.15), we have
Comparison of (6.14) and (6.16) indicates they are correct through the first three terms.
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 146/30/2014
21
21
1 s
s
(s)Ge s
(6.15)
...4
2
1
3322
ssse s (6.16)
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12
s
2
s1
12
s
2
s1
)(22
22
2
sGe s (6.17)
Comparison of actual
and approximate time
delay responses
Processes with Time Delays
2/2 Pad approximation
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 156/30/2014
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An alternative first-order approximation consists of the transfer function,
where the time constant has a value of 0
These expressions can be used to approximate the pole or zero term in a transfer function.
0
0
0
1 1(6-58)
1
s
se
se
Processes with Time Delays
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 166/30/2014
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Conclusions
Interacting and non-interacting systems were introduced
Transfer functions for higher order systems have been derived
Delay time concept has been introduced.
Transfer function and approximations are explained.
CCB 3013 - Chemical Process Dynamics, Instrumentation and Control 176/30/2014