A A 1 c 1 2 1 If ; ; K ; K 1 2 1 2 c c - - PowerPoint PPT Presentation

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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 )


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Department of Chemical Engineering I.I.T. Bombay, India

) ( 1 ) ( ) ( ; 1 ; c A ; c A If

1 2 2 1 2 2 1 2 1 2 2 1 2 1 1 2 2 2 1 1 1

s u s K s K K s y c c K c K                

First Principles Model The roots of the denominator (poles of the transfer function) could be complex. They could give rise to oscillatory behaviour for different u.

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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

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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

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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

   

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

    w w