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Dead Time Compensation

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Chapter 3 Dead Time Compensation Smith Predictor, A Model Based Approach 1. Effects of Dead-Time (Time Delay) Process with large dead time (relative to the time ... – PowerPoint PPT presentation

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Title: Dead Time Compensation


1
Chapter 3
  • Dead Time Compensation Smith Predictor, A Model
    Based Approach

2
1. Effects of Dead-Time (Time Delay)
  • Process with large dead time (relative to the
    time constant of the process) are difficult to
    control by pure feedback alone
  • Effect of disturbances is not seen by controller
    for a while
  • Effect of control action is not seen at the
    output for a while. This causes controller to
    take additional compensation unnecessary
  • This results in a loop that has inherently built
    in limitations to control

3
Example A Bode Plot Example
htf(1,1 3 3 1,'inputdelay',1)
4
Example- continued, case without time delay
5
PID Control Results- Case with delay
(Kc1,Ki1,Kd1)
6
PID Control Results- Case without delay
(Kc1,Ki1,Kd1)
7
2. Causes of Dead-Time
  • Transportation lag (long pipelines)
  • Sampling downstream of the process
  • Slow measuring device GC
  • Large number of first-order time constants in
    series (e.g. distillation column)
  • Sampling delays introduced by computer control

8
3. The Smith Predictor
9
Control with Smith Predictor (Kc1,Ki1,Kd1)
10
Alternate form
11
Example 2 Long time delay
1 G(s)
exp(-3s) ---------------------
s3 3 s2 3 s 1

Mag-3.3dB20log10(AR) AR0.6839 Wu0.5Pu2p/0.
512.5664 Ku1/0.68391.4622 Kc0.8601 TauiPu/26
.2832 TaudPu/81.5708
12
Load Disturbance Response
13
The Effect of Modeling Error
Errors in td,G both cause the control system to
degrade
14
Smith Predictor with Modeling Error
Plante-s/(s33s23s1)
Modele-s/(s3s2s1)
Modele-0.5s/(s3s2s1)
15
Analytical Predictor
y(s)
GC(s)
GPe-DS
ySP
Analytical Predictor
y(tD)
Analytical Predictor is a model that projects
what y will be D units into the future (on-line
model identification)
16
Processes with inverse response
The output goes to the wrong way first
Example This can occurs in (1) reboiler level
response to change in heat input to the
reboiler. (2) Some tubular reactor exist
temperature To inlet flow rate . Inverse response
is caused by a RHP zero
17
Example Inverse response of concentration and
temperature to a chanbe in process flow of 0.15
ft3/min
18
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20
Open Loop Response Analysis
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