+ All Categories
Home > Documents > L10 - Chapter 3

L10 - Chapter 3

Date post: 22-Jul-2016
Category:
Upload: syed-nazrin
View: 23 times
Download: 3 times
Share this document with a friend
Description:
good
27
Laplace Transform CCB3013 - Chemical Process Dynamics, Instrumentation and Control 1 6/16/2014 Chapter 3 Laplace Transform
Transcript
Page 1: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 16/16/2014

Chapter 3

Laplace Transform

Page 2: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 26/16/2014

Chapter Objectives

End of this chapter, you should be able to:

• Use Laplace Transform of representative functions

• Solve differential equations by Laplace Transform

techniques

• Explain other Laplace Transform properties

– Final value theorem

– Initial value theorem

– Time delay (translation in time)

Page 3: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 36/16/2014

3.1 Laplace Transform of Representative

Functions

The Laplace transform of a function f(t) is defined as

0

)()]([)( dtetf =tfLsF -st

(3.1)

where F(s) is the symbol for the Laplace transform

s is a complex independent variable

f(t) is some function of time

Page 4: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 46/16/2014

Transforms of some important functions

Constant function: f(t) = a

s

a

s

ae

s

adtae=aL st-st

0][0

0

(3.2)

Page 5: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 56/16/2014

Transforms of some important functions

Step function:

The unit step function is defined as

0 1

0 0)(

t

ttS (3.3)

The Laplace transform of the unit step function is

obtained with a = 1

stSL

1)]([ (3.4)

Page 6: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 66/16/2014

Transforms of some important functions

Exponential Functions

bteb > 0

bs

esb

dtedtee=eL tsbtsb-stbtbt

11

][0

)(

0

)(

0

(3.5)

Page 7: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 76/16/2014

Transforms of some important functions

Derivatives

)0()()0(][

)()(

][

00

0

fssFffsL

etfsdtetf

dtedtdf=dtdfL

stst

-st

(3.6)

Usually define f(0) = 0

Page 8: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 86/16/2014

Transforms of some important functions

Second-order derivatives

dt

dL

dt

fdL

2

2

wheredt

df

)0()0()(

)0()0()(

)0()(

2

2

2

fsfsFs

ffssFs

ss

dt

dL

dt

fdL

(3.7)

Page 9: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 96/16/2014

Transforms of some important functions

Higher-order derivatives

)0()0(

...)0()0()(

)1()2(

21

nn

nnn

n

n

fsf

fsfssFsdt

fdL

(3.8)

Page 10: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 106/16/2014

Transforms of some important functions

Trigonometric functions

Euler identity:2

costjtj ee

t

cos sin

cos sin

1

j t

jwt

e t j t

e t j t

j

Page 11: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 116/16/2014

Transforms of some important functions

Cosine function

22

222

1

11

2

1

2cos

s

s

s

jsjs

jsjs

eeLtL

tjtj

Page 12: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 126/16/2014

Transforms of some important functions

Sine function

22

222

1

11

2

1

2sin

s

s

jsjs

j

jsjsj

j

eeLtL

tjtj

(3.9)

Page 13: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 136/16/2014

Rectangular pulse function

0

1 1( ) (1 )

hst hsF s e dt e

h hs

ht

htht

tf

0

0 /10 0

)( (3.10)

Page 14: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 146/16/2014

Rectangular pulse function

If h = 1, unit rectangular pulse input.

Difference of two step inputs S(t) – S(t-1). (S(t-1) is a

step starting at t = h = 1)

By Laplace transform

1( )

seF s

s s

Can be generalized to steps of different magnitudes (a1, a2).

Page 15: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 156/16/2014

Impulse function

Let h→0, f(t) = δ(t) (Dirac delta) L(δ) = 1

Laplace transforms can be used in process control for:

• Solution of differential equations (linear)

• Analysis of linear control systems (frequency

response

• Prediction of transient response for different inputs

Page 16: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 166/16/2014

General procedure for solving differential

equations

repeated factors

and complex

factors may arise.

Page 17: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 176/16/2014

Example 3.1 Solve the ODE,

5 4 2 0 1 (3-26)dy

y ydt

(3.11)

First, take L of both sides of (3-11),

2

5 1 4sY s Y ss

Rearrange,

5 2

(3-34)5 4

sY s

s s

(3.12)

Take L-1,

1 5 2

5 4

sy t

s s

L

From L Table

0.80.5 0.5 (3-37)ty t e (3.13)

Page 18: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 186/16/2014

Example 3.2

00

0000

2461162

2

3

3

at t=dt

du

)=(y)=(y)=y(

udt

duy

dt

dy

dt

yd

dt

yd

To find transient response for u(t) = unit step at t > 0 :

1. Take Laplace Transform (L.T.)

2. Factor, use partial fraction decomposition

3. Take inverse L.T.

Page 19: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 196/16/2014

Step 1 Take L.T. (note zero initial conditions)

3 26 11 6 ( ) 4 2s Y(s)+ s Y(s)+ sY(s) Y s = sU(s) + U(s)

Rearranging,

input) (1

1

6116

2423

stepunits

U(s)

ssss

s+Y(s)=

Step 2a. Factor denominator of Y(s)

))(s+)(s+)=s(s+s++s+s(s 3216116 23

Page 20: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 206/16/2014

Step 2b. Use partial fraction decomposition

321321

24 4321

s

α

s

α

s

α

s

α

))(s+)(s+s(s+

s+

Multiply by s, set s = 0

3

1

321

2

321321

24

1

0

4321

0

α

s

α

s

α

s

αsα

))(s+)(s+(s+

s+

ss

For a2, multiply by (s+1), set s = -1 (same procedure for a3, a4)

3

531 432 , α, αα

3

3/5

2

3

1

1

3

1

ssssY(s)=

Page 21: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 216/16/2014

Step 3. Take inverse of L.T.

3

1

3

53

3

1 32

) y(tt

eeey(t)= ttt

Page 22: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 226/16/2014

Dynamic Analysis

2

2

3 4 1s s

Example 1:2 16

1.333 14 12

b

a

2 13 4 1 (3 1)( 1) 3( )( 1)3

s s s s s s

Transforms to e-t/3, e-t (real roots) - (no oscillation)

2

2

1

s

s s

Example 2:

2 11

4 4

b

a

2 3 31 ( 0.5 )( 0.5 )

2 2s s s j s j

Transforms to 0.5 0.53 3

sin , cos2 2

t te t e t

(oscillation)

Page 23: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 236/16/2014

Remarks

• You can use this method on any order of ODE, limited only

by factoring of denominator polynomial (characteristic

equation)

• Must use modified procedure for repeated roots,

imaginary roots

One other useful feature of the Laplace transform is that one

can analyze the denominator of the transform to determine its

dynamic behavior. For example, if

23

12 ss

Y(s)=

the denominator can be factored into (s+2)(s+1).

Page 24: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 246/16/2014

Remarks

Using the partial fraction technique

12

21

s

α

s

αY(s)=

The step response of the process will have exponential

terms e-2t and e-t, which indicates y(t) approaches zero.

))(s(sssY(s)=

21

1

2

12

However, if

• We know that the system is unstable and has a transient

response involving e2t and e-t. e2t is unbounded for large

time.

• We shall use this concept later in the analysis of

feedback system stability.

Page 25: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 256/16/2014

Other properties of L( ):

A. Final value theorem

sY(s))=y(s 0lim

“offset”

Example 3: Step response

aτs

a

τs

asY(s)

s

a

τsY(s)

s

1lim

1

1

1

0

offset (steady state error) is a.

Page 26: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 266/16/2014

Other properties of L( ):

Time-shift theorem

y(t)=0 t < Y(s)=et-yL s-

Initial value theorem

sY(s)y(t)=st limlim

0

Example 4.

)3)(2)(1(

24)(

s+s+s+s

s+=sFor Y

by initial value theorem: 0)0( y

by final value theorem:3

1)( y

Page 27: L10 - Chapter 3

Lap

lace T

ran

sfo

rm

CCB3013 - Chemical Process Dynamics, Instrumentation

and Control 276/16/2014

Conclusion!

• Laplace transform definition

• Laplace transform of some typical functions

• Inverse Laplace transforms

• Examples

• Dynamic Analysis


Recommended