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Control Systems
Prof. C. S. Shankar Ram
Department of Engineering Design
Indian Institute of Technology, Madras
Lecture – 07
Transfer Function
Part – 1
We are dealing with single input single output systems abbreviated as SISO and linear
time invariant causal dynamic systems that are characterized by linear ordinary
differential equations with the constant coefficients.
(Refer Slide Time: 00:28)
We have looked at how one could use the Laplace transform to solve such equations.
What we have done till now is to have a broad overview of what we are going to study in
this course and some mathematical tools that we are going to use.
(Refer Slide Time: 00:49)
We will go into the analysis using the classical control approach. One of the main topics
that we are going to learn is that of transfer functions. Let us see what a transfer function
is. Let us consider the mass spring damper system that is governed by
𝑀𝑥( 𝑡)̈ + 𝐶𝑥( 𝑡)̇ + 𝐾𝑥( 𝑡) = 𝑓( 𝑡)
This is a linear time invariant system. Let us take the Laplace transform on both sides,
we are going to get
𝑀[ 𝑠2
𝑋( 𝑠) − 𝑠𝑥(0) − 𝑥̇(0)] + 𝐶[ 𝑠𝑋( 𝑠) − 𝑥(0)] + 𝐾𝑋( 𝑠) = 𝐹( 𝑠)
If we just rearrange the terms we are going to get
[ 𝑀𝑠2
+ Cs + K] 𝑋( 𝑠) = [ 𝑀𝑠 + 𝐶] 𝑥(0) + 𝑀𝑥̇(0) + 𝐹( 𝑠)
If we now divide both sides by 𝑀𝑠2
+ Cs + K we are going to get the following.
𝑋( 𝑠) =
[ 𝑀𝑠 + 𝐶] 𝑥(0) + 𝑀𝑥̇(0)
[ 𝑀𝑠2 + Cs + K]
+
𝐹(𝑠)
[ 𝑀𝑠2 + Cs + K]
The first term is the component of the output is due to the non-zero initial condition. One
could immediately observe that it involves 𝑥(0) and 𝑥̇(0). That is the displacement
which is caused by any non-zero initial condition. If we have the mass initially at rest,
we displace it by a small amount and leave it, it may vibrate depending on the values of
K and C and finally, it may settle down back to it is originally equilibrium state. The first
part is the output due to non zero initial conditions. We call it as a free response.
The second part involves the input term 𝐹(𝑠), which is the force. Suppose we apply a
time varying force on the mass, the second term provides us the displacement of the
mass. That is the contribution of the input force to the output. We call it as the forced
response. We are going to have these two components to the output. One due to non-zero
initial conditions and other due to the input that is provided to the system.
(Refer Slide Time: 07:42)
Now, let us consider all initial conditions to be 0. In this case 𝑥(0) = 0 and 𝑥̇(0) = 0.
Then
𝑋( 𝑠) =
𝐹(𝑠)
[ 𝑀𝑠2 + Cs + K]
𝑋( 𝑠)
𝐹( 𝑠)
=
1
[ 𝑀𝑠2 + Cs + K]
So, this quantity (
𝑋(𝑠)
𝐹(𝑠)
) which is the ratio of the Laplace transform of the output to the
Laplace transform of the input under 0 initial conditions is called as the transfer function
of the system or plant. We will use 𝑃(𝑠) to denote the transfer function. To summarize,
we wrote down the governing linear ordinary differential equation, then we took Laplace
transform on both sides, we saw that the output term has two components one due to the
non-zero initial conditions and one due to the input. We took all initial conditions to be
0. Then, we took the ratio of the Laplace of the output to the Laplace of the input, which
is called as the transfer function of the system or the plant and we are going to denote by
(𝑠). In a certain sense when we use the transfer function approach we are interested in
the forced response of the system because we have taken all initial conditions to be 0.
Now the question becomes will initial conditions be zero all the time in practice? If not
what would happen if we follow this approach? That is a question we would answer
later.
Please remember that, we can take ratios of Laplace of output and input only if we have
a SISO system. If we have a MIMO system, we would have a transfer function matrix.
We can no longer divide a vector output by a vector input. We can still write it in another
product form, where we can say the output vector is going to be equal to a transfer
function matrix multiplying an input vector in the complex domain.
But we are going to deal with single input single output systems in this course. So, the
notations followed holds through for a single input single output system. Consequently,
𝑌( 𝑠) = 𝑃( 𝑠) 𝑈( 𝑠).
(Refer Slide Time: 14:26)
If we take the inverse Laplace transform, we have
𝑦( 𝑡) = ∫ 𝑝( 𝑡 − 𝜏) 𝑢( 𝜏) 𝑑𝜏
𝑡
0
,
𝑦(𝑡) is the output in the time domain if we take the inverse Laplace transform. We can
note certain points. The first point is, if 𝑃(𝑠) is known, we can find the system output for
any input. Another thing we can do is, if we want some output we can find out what
input to give. We can do both control and analysis, what we studied as purpose of
models. Prediction or analysis is where we have an input and we evaluate the output.
Control is where we have a desired output and we find the input to be given. The second
point is, if 𝑢(𝑡) is the unit impulse input, then 𝑈( 𝑠) = 1. Therefore 𝑌( 𝑠) = 𝑃(𝑠), this
implies that 𝑦( 𝑡) = 𝑝(𝑡)
If you give any input and you calculate the corresponding output, that output is called as
a response and the adjective can be added which corresponds to that specific input. In
this particular case we are providing a unit impulse input to the system. So, consequently
the output that we get is called as the impulse response and 𝑝(𝑡) is the impulse response
function. And the Laplace of the impulse response function 𝑝(𝑡) is the plant transfer
function 𝑃(𝑠).
This gives us a very useful idea, if we want to experimentally determine the plant
transfer function, we just need to give a unit impulse input and then measure what is the
output and that will be the impulse response function. From the impulse response
function, we can calculate the plant transfer function. The advantage is we need to do
only one experiment, but the catch here is, in practice it is very difficult to give an ideal
impulse input. Then the question becomes, what approximations can we get? Is there any
other method to figure out the transfer functions? We will learn as we progress. There is
another method by which we can experimentally determine transfer functions by using
frequency response, ok. So, we would learn that technique also. At the end of the day, if
we want to figure out a plant transfer function it is going to be a mix of both approaches.
For example, it is going to be a mix of deriving equations based on physics and also
performing experiments and using experimental data to fit the transfer function, we need
both approaches.
As far as the definition of the transfer function is concerned it is extremely important that
we keep all initial conditions to be 0, then only we can talk about transfer functions and
use them.

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Lec7

  • 1. Control Systems Prof. C. S. Shankar Ram Department of Engineering Design Indian Institute of Technology, Madras Lecture – 07 Transfer Function Part – 1 We are dealing with single input single output systems abbreviated as SISO and linear time invariant causal dynamic systems that are characterized by linear ordinary differential equations with the constant coefficients. (Refer Slide Time: 00:28) We have looked at how one could use the Laplace transform to solve such equations. What we have done till now is to have a broad overview of what we are going to study in this course and some mathematical tools that we are going to use.
  • 2. (Refer Slide Time: 00:49) We will go into the analysis using the classical control approach. One of the main topics that we are going to learn is that of transfer functions. Let us see what a transfer function is. Let us consider the mass spring damper system that is governed by 𝑀𝑥( 𝑡)̈ + 𝐶𝑥( 𝑡)̇ + 𝐾𝑥( 𝑡) = 𝑓( 𝑡) This is a linear time invariant system. Let us take the Laplace transform on both sides, we are going to get 𝑀[ 𝑠2 𝑋( 𝑠) − 𝑠𝑥(0) − 𝑥̇(0)] + 𝐶[ 𝑠𝑋( 𝑠) − 𝑥(0)] + 𝐾𝑋( 𝑠) = 𝐹( 𝑠) If we just rearrange the terms we are going to get [ 𝑀𝑠2 + Cs + K] 𝑋( 𝑠) = [ 𝑀𝑠 + 𝐶] 𝑥(0) + 𝑀𝑥̇(0) + 𝐹( 𝑠) If we now divide both sides by 𝑀𝑠2 + Cs + K we are going to get the following. 𝑋( 𝑠) = [ 𝑀𝑠 + 𝐶] 𝑥(0) + 𝑀𝑥̇(0) [ 𝑀𝑠2 + Cs + K] + 𝐹(𝑠) [ 𝑀𝑠2 + Cs + K] The first term is the component of the output is due to the non-zero initial condition. One could immediately observe that it involves 𝑥(0) and 𝑥̇(0). That is the displacement which is caused by any non-zero initial condition. If we have the mass initially at rest, we displace it by a small amount and leave it, it may vibrate depending on the values of
  • 3. K and C and finally, it may settle down back to it is originally equilibrium state. The first part is the output due to non zero initial conditions. We call it as a free response. The second part involves the input term 𝐹(𝑠), which is the force. Suppose we apply a time varying force on the mass, the second term provides us the displacement of the mass. That is the contribution of the input force to the output. We call it as the forced response. We are going to have these two components to the output. One due to non-zero initial conditions and other due to the input that is provided to the system. (Refer Slide Time: 07:42) Now, let us consider all initial conditions to be 0. In this case 𝑥(0) = 0 and 𝑥̇(0) = 0. Then 𝑋( 𝑠) = 𝐹(𝑠) [ 𝑀𝑠2 + Cs + K] 𝑋( 𝑠) 𝐹( 𝑠) = 1 [ 𝑀𝑠2 + Cs + K] So, this quantity ( 𝑋(𝑠) 𝐹(𝑠) ) which is the ratio of the Laplace transform of the output to the Laplace transform of the input under 0 initial conditions is called as the transfer function of the system or plant. We will use 𝑃(𝑠) to denote the transfer function. To summarize, we wrote down the governing linear ordinary differential equation, then we took Laplace transform on both sides, we saw that the output term has two components one due to the
  • 4. non-zero initial conditions and one due to the input. We took all initial conditions to be 0. Then, we took the ratio of the Laplace of the output to the Laplace of the input, which is called as the transfer function of the system or the plant and we are going to denote by (𝑠). In a certain sense when we use the transfer function approach we are interested in the forced response of the system because we have taken all initial conditions to be 0. Now the question becomes will initial conditions be zero all the time in practice? If not what would happen if we follow this approach? That is a question we would answer later. Please remember that, we can take ratios of Laplace of output and input only if we have a SISO system. If we have a MIMO system, we would have a transfer function matrix. We can no longer divide a vector output by a vector input. We can still write it in another product form, where we can say the output vector is going to be equal to a transfer function matrix multiplying an input vector in the complex domain. But we are going to deal with single input single output systems in this course. So, the notations followed holds through for a single input single output system. Consequently, 𝑌( 𝑠) = 𝑃( 𝑠) 𝑈( 𝑠). (Refer Slide Time: 14:26) If we take the inverse Laplace transform, we have 𝑦( 𝑡) = ∫ 𝑝( 𝑡 − 𝜏) 𝑢( 𝜏) 𝑑𝜏 𝑡 0 ,
  • 5. 𝑦(𝑡) is the output in the time domain if we take the inverse Laplace transform. We can note certain points. The first point is, if 𝑃(𝑠) is known, we can find the system output for any input. Another thing we can do is, if we want some output we can find out what input to give. We can do both control and analysis, what we studied as purpose of models. Prediction or analysis is where we have an input and we evaluate the output. Control is where we have a desired output and we find the input to be given. The second point is, if 𝑢(𝑡) is the unit impulse input, then 𝑈( 𝑠) = 1. Therefore 𝑌( 𝑠) = 𝑃(𝑠), this implies that 𝑦( 𝑡) = 𝑝(𝑡) If you give any input and you calculate the corresponding output, that output is called as a response and the adjective can be added which corresponds to that specific input. In this particular case we are providing a unit impulse input to the system. So, consequently the output that we get is called as the impulse response and 𝑝(𝑡) is the impulse response function. And the Laplace of the impulse response function 𝑝(𝑡) is the plant transfer function 𝑃(𝑠). This gives us a very useful idea, if we want to experimentally determine the plant transfer function, we just need to give a unit impulse input and then measure what is the output and that will be the impulse response function. From the impulse response function, we can calculate the plant transfer function. The advantage is we need to do only one experiment, but the catch here is, in practice it is very difficult to give an ideal impulse input. Then the question becomes, what approximations can we get? Is there any other method to figure out the transfer functions? We will learn as we progress. There is another method by which we can experimentally determine transfer functions by using frequency response, ok. So, we would learn that technique also. At the end of the day, if we want to figure out a plant transfer function it is going to be a mix of both approaches. For example, it is going to be a mix of deriving equations based on physics and also performing experiments and using experimental data to fit the transfer function, we need both approaches. As far as the definition of the transfer function is concerned it is extremely important that we keep all initial conditions to be 0, then only we can talk about transfer functions and use them.