Lecture 5 PPT
Page 1 — Agenda
The lecture covers 3 major topics:
- First-order systems
- Integrating systems
- Linearization
These are some of the most fundamental system models in control theory.
Think of this lecture as teaching you:
- how systems respond over time
- how to model them mathematically
- how to simplify nonlinear real-world systems
Page 2 — Closed Loop Transfer Function
This is one of the most important formulas in control engineering.
The slide shows a feedback control loop:
R(s) \rightarrow D(s) \rightarrow G(s) \rightarrow Y(s)
with feedback through (H(s))
Where:
- (R(s)) = reference / desired value
- (Y(s)) = actual output
- (D(s)) = controller
- (G(s)) = process / plant
- (H(s)) = sensor / feedback
- (E(s)) = error = desired − measured
The key formula:
\frac{Y(s)}{R(s)} = \frac{D(s)G(s)}{1 + D(s)G(s)H(s)}
This is the closed-loop transfer function.
What does this mean intuitively?
This tells us:
“How does the output respond to the input when feedback is active?”
This is much more realistic than open-loop systems because most real systems use feedback.
Examples:
- thermostat
- cruise control
- autopilot
- motor speed control
Why feedback matters
Without feedback: the system just acts blindly
With feedback: the system constantly checks:
“Am I at the target yet?”
That’s why control systems are powerful.
Page 3 — Idealized Process Inputs
This page introduces standard test signals.
These are very important because we use them to test how systems behave.
Two main signals:
Step input
u(t)=A
after time (t_0)
This means the input suddenly jumps.
Example:
- turning on heater power instantly
- switching motor voltage from 0V to 5V
This is the most common test signal.
Laplace transform:
U(s)=\frac{A}{s}
Impulse input
This is a very short “shock” input:
\delta(t)
It happens instantaneously.
Examples:
- hammer hit
- sudden pulse of force
- electrical spike
Laplace transform:
\delta(s)=1
Very important.
Page 4 — Ramp Input
Ramp means the signal increases linearly over time.
u(t)=at
This is like a straight line.
Examples:
- temperature increasing steadily
- speed increasing constantly
- filling tank at constant acceleration
Laplace:
U(s)=\frac{a}{s^2}
Intuition
Step = sudden jump Ramp = gradual linear increase
This difference strongly affects system response.
Page 5 — Metal Block Heating Example
This is a beautiful physical example of a first-order system.
The differential equation:
Mc\frac{dT_m}{dt}=P_-hA(T_m-T_s)
This is just an energy balance.
Left side
Mc\frac{dT_m}{dt}
This means:
rate of temperature change × thermal mass
So it represents stored heat energy.
Right side
Input heating power:
P_
Heat loss:
hA(T_m-T_s)
This means heat escapes to surroundings.
Very realistic model.
Transfer function
After Laplace transform:
\frac{T_m(s)}{P_(s)}=\frac{K}{\tau s+1}
This is the classic first-order transfer function.
Extremely important.
Page 6 — General First Order System
This is the general form:
\frac{dy}{dt}=Au-\alpha y
This means:
- input pushes output upward
- output naturally decays downward
Very common in physics and engineering.
Transfer function
G(s)=\frac{K}{\tau s+1}
This is the universal first-order model.
Examples:
- temperature
- liquid flow
- RC circuits
- motor speed
- concentration systems
Important concepts
Gain (K)
Final system amplification
Bigger (K) = bigger final output
Time constant (\tau)
Extremely important.
This tells you how fast the system responds.
Small (\tau) = fast system Large (\tau) = slow system
Page 7 — Step Response of First Order System
For step input:
y(t)=K(1-e^{-t/\tau})
This equation is one of the most important in control.
What shape is this?
An exponential rise curve.
Starts fast, then slows down.
Exactly like:
- heating room
- charging capacitor
- filling pressure tank
Important points
At:
t=\tau
system reaches:
63%
of final value
This is VERY important.
You must remember this.
Page 8 — Graph Explanation
This graph explains all timing parameters.


Time constant
At one (\tau):
63%
At 4τ:
almost fully settled
Rise time
T_r=2.2\tau
Time from 10% → 90%
Settling time
T_s=4\tau
Time until stable within ±2%
This is used everywhere in control design.
Page 9 — Impulse Response
For impulse input:
u(s)=1
Response becomes:
y(t)=\frac{K_p}{\tau_p}e^{-t/\tau_p}
This is exponential decay.
Meaning
Impulse gives sudden peak response that decays.
Like hitting a spring.
Very common in system identification.
Page 10 — Ramp Response
For ramp:
u(s)=\frac{1}{s^2}
The output lags behind the ramp.
Important idea:
first-order systems cannot instantly follow changing inputs
They always have delay.
Page 11 — Integrating Systems
This is the second major topic.
\dot{C}(t)=KU(t)
Meaning:
output is integral of input
C(t)=\int U(t)dt
Very intuitive meaning
If input stays positive, output keeps growing forever.
Unlike first-order systems, it does NOT saturate.
Examples
Car
velocity → integrated gives position
x(t)=\int v(t)dt
Tank
flow → integrated gives volume
V(t)=\int f_(t)dt
Very important.
Page 12 — Tank Without Outlet
This is a pure integrator.
Constant inflow gives:
l(t)=\frac{1}{\rho A}t
This means level increases linearly forever.
This is exactly what the graph should look like.
Straight line.
Page 13 — Feedback on Integrator
Very important concept.
When feedback is added:
\frac{K}{s+K}
Suddenly the integrator behaves like a first-order system
This is super important in control design.
Feedback stabilizes integrating systems.
Pages 14–15 — Experimental Parameter Estimation
These slides show how to determine system parameters from real data.
This is system identification.
First-order
From graph:
- final value → gain
- 63% point → τ
Example:
G(s)=\frac{9}{4s+1}
Integrator
Slope gives gain
K=\frac{\Delta y}{\Delta t}
Very practical engineering method.
Page 17–20 — Why Linearization?
This is one of the most important theory parts.
Laplace methods require linear equations.
But real systems are often nonlinear.
So we approximate them locally as linear.
This is called linearization.
Page 21 — Nonlinear Equations
Examples:
5y^2+\sqrt{u}
yu
These are nonlinear because variables multiply or are squared.
Laplace cannot directly solve these.
Pages 23–29 — Linearization (VERY IMPORTANT)
This is Taylor approximation around an operating point.
Core idea:
Approximate nonlinear curve by tangent line locally.


Main idea
Near operating point:
(\bar{y},\bar{u})
small changes:
\hat{y}=y-\bar{y}
\hat{u}=u-\bar{u}
Then system becomes approximately linear.
Why useful?
Because then we can use:
- Laplace
- transfer functions
- control design
This is the foundation of modern control.
Pages 30–34 — Room Temperature Example
This is a full practical example.
Very nice slide.
The room behaves as first-order thermal system.
Model
cm\frac{dT}{dt}=P-hA(T-T_0)
This is exactly same as metal block.
Input:
heater power
Output:
room temperature
Linearization
They define:
\hat{T}=T-20
Meaning:
temperature deviation from 20°C
This makes equation linear.
Very common engineering trick.
Step response
For 1000 W heater:
temperature rises exponentially.
Graph shows room slowly approaching steady state.
Very realistic.
Page 35 — Final Control Structure
Very important concept.
Controller works on small signal deviations, not absolute values.
This is how real controllers are often designed.
Example:
maintain room at 22°C
controller only reacts to deviation from 22°C.
Big Picture Summary
This lecture teaches 3 absolutely core control concepts:
1) First-order systems
\frac{K}{\tau s+1}
Exponential response
63% at τ
2) Integrators
\frac{K}{s}
Output keeps increasing
3) Linearization
Approximate nonlinear systems near operating point
Enables Laplace + control design
This is one of the most foundational lectures in control engineering.