Title: Dead Time Compensation
1Chapter 3
- Dead Time Compensation Smith Predictor, A Model
Based Approach
21. 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
3Example A Bode Plot Example
htf(1,1 3 3 1,'inputdelay',1)
4Example- continued, case without time delay
5PID Control Results- Case with delay
(Kc1,Ki1,Kd1)
6PID Control Results- Case without delay
(Kc1,Ki1,Kd1)
72. 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
83. The Smith Predictor
9Control with Smith Predictor (Kc1,Ki1,Kd1)
10Alternate form
11Example 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
12Load Disturbance Response
13The Effect of Modeling Error
Errors in td,G both cause the control system to
degrade
14Smith Predictor with Modeling Error
Plante-s/(s33s23s1)
Modele-s/(s3s2s1)
Modele-0.5s/(s3s2s1)
15Analytical 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)
16Processes 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
17Example Inverse response of concentration and
temperature to a chanbe in process flow of 0.15
ft3/min
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20Open Loop Response Analysis