Instrumentation

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.

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