Department of Chemical Engineering I.I.T. Bombay, India
A A 1 c 1 2 1 If ; ; K ; K 1 2 1 2 c c - - PowerPoint PPT Presentation
A A 1 c 1 2 1 If ; ; K ; K 1 2 1 2 c c - - PowerPoint PPT Presentation
Department of Chemical Engineering I.I.T. Bombay, India First Principles Model A A 1 c 1 2 1 If ; ; K ; K 1 2 1 2 c c c c 1 2 1 2 K K 1 2 y ( s ) u ( s )
Department of Chemical Engineering I.I.T. Bombay, India
Second Illustrative example: Control of a first order process
Ku y dt dy
t d I d c
dt y y y y K t u ) ( 1 ) ( ) (
and
t d I d c
dt y y y y KK y dt dy ) ( 1 ) (
Therefore,
d I c c
y y KK dt dy KK dt y d ) 1 (
2 2 1
This is a second order system and will give rise to a second
- rder transfer function.
Plant controller yd +
- y
u
Department of Chemical Engineering I.I.T. Bombay, India
plane of initial rest when DP = 0 h h P1 P2 DP = P1 - P2
U-Tube Manometer
P g h dt dh R g L dt h d g L D 2 1 4 2
2 2 2
L = length of fluid in the manometer tube , = density and viscosity
- f manometer fluid
R = radius of manometer tube g = gravitation constant
Department of Chemical Engineering I.I.T. Bombay, India
General second order transfer function
1 2 ) ( ) ( ) (
2 2
s s K s u s y s G
The value of (damping factor) determines the dynamic response of second order systems. It represents viscous or dissipative forces. If 0 < 1 (underdamped system) - oscillatory approach to steady state 1 (critically damped, overdamped systems) - non-oscillatory approach to steady state. is also called the natural time constant of the system. For the manometer
3 2 g L g L R 6
2
Department of Chemical Engineering I.I.T. Bombay, India
Step Response of Overdamped Second Order Systems
s A s u ) (
2 1 / 2 / 1
2 1
1 ) (
t t
e e KA t y
2 1 / /
2 1
t t
e e KA dt dy
= 0 at t= 0 Initial Slope = 0. This is in contrast to that of a first order system
Department of Chemical Engineering I.I.T. Bombay, India
Step Response of Critically Damped Second Order Systems
s A s u ) (
= 0 at t= 0 Again, the initial Slope = 0
/
1 1 ) (
t
e t KA t y
2 /
t
e t KA dt dy
Department of Chemical Engineering I.I.T. Bombay, India
Step Response of Underdamped Second Order Systems
s A s u ) (
= 0 at t= 0 Again, the initial Slope = 0
t t e KA t y
t
2 2 2 /
1 sin 1 1 cos 1 ) (
2 2 /
1 1 sin
t e KA dt dy
t
Department of Chemical Engineering I.I.T. Bombay, India
tr
Rise time tr: Time at which the output first hits the steady state value
) cos ( 1
1 2
r
t
Step Response of Underdamped Second Order Systems
Department of Chemical Engineering I.I.T. Bombay, India
Time to first peak tp: Time at which the output hits the first maximum value
tp Peak time
Department of Chemical Engineering I.I.T. Bombay, India
a a = max(y) - D y b = D y b
) 1 exp(
2
OS
Overshoot (OS) = a / b
Department of Chemical Engineering I.I.T. Bombay, India
ts b = D y
0.95 * b 1.05 * b Time taken to reach and remain within 5% of the total change in y (95% response time)
Settling time
Department of Chemical Engineering I.I.T. Bombay, India
a a = value of first peak - D y c = value of second peak - D y Decay ratio (DR) = c / a c
) 1 2 exp(
2 2
OS DR
Department of Chemical Engineering I.I.T. Bombay, India
Period of Oscillation, P = time between successive peaks = time between successive valleys
P
2 2 /
1 1 sin
t e KA dt dy
t
2
1 2 P
Department of Chemical Engineering I.I.T. Bombay, India
Frequency Response
1 2 ) ( ) ( ) (
2 2
s s K s u s y s G
with ) sin( ) ( wt A s u It can be shown that the output y is also a sinusoid with the same frequency as the input and is given by, ) sin( ) 2 ( ) 1 ( ) (
2 2 2 2
wt w w AK t y
t
and
) 1 ( 2 tan
2 2 1