Instrumentation

Chapter 6: Dynamic Behavior of Ideal Systems

This chapter covers the most important “ideal” system models used in engineering and control:

  • ideal inputs
  • first-order systems
  • second-order systems
  • integrating systems
  • high-order systems
  • deadtime
  • FOPDT models

These are the core models used to approximate real industrial systems.

Examples:

  • tank level
  • reactor temperature
  • flow systems
  • chemical concentrations
  • mechanical systems

1) Idealized Process Inputs

Before understanding the system response, we first need to understand the types of input signals.

This is extremely important because the same system behaves differently depending on the input.


A) Impulse input

This is a very short but very strong input.

Imagine injecting dye instantly into a tank.

The input is almost like a spike:

  • huge magnitude
  • almost zero duration
  • finite total area

Visually:

  • one sharp vertical spike

The area under it equals 1 for a unit impulse.


Intuition

This is used to study how the system reacts to a sudden shock.

Examples:

  • sudden salt injection
  • pulse of energy
  • electrical spike

This is often used for system identification.


B) Step input

This is the MOST important input in control engineering.

A step means:

the input suddenly changes and stays there.

Example:

flow changes from 5 L/min → 8 L/min instantly

Like flipping a switch.

This is what most examples in the chapter use.


C) Pulse input

A pulse is like a temporary step.

Input rises suddenly, then returns back after some time.

Example:

  • inject salt for 5 seconds
  • stop injection

Very useful for tracer studies.


D) Ramp input

A ramp means the input increases continuously with time.

Example:

temperature increases steadily:

20°C → 25°C → 30°C → 35°C

This is common in industrial heating systems.


E) Sinusoidal input

This is periodic oscillation.

Like:

u(t)=A\sin(\omega t)

Examples:

  • day/night temperature cycles
  • AC electrical signals
  • vibration systems

This is very important in frequency response analysis.


2) First-Order Processes

This is probably the MOST important model in this chapter.

A first-order system has this differential equation:

\tau_p \frac{dy}{dt}+y=K_pu

\tau_p \frac{dy}{dt}+y=K_pu

Where:

  • (y(t)) = output
  • (u(t)) = input
  • (K_p) = process gain
  • (\tau_p) = time constant

What does this mean physically?

A first-order system responds smoothly and exponentially.

It does NOT jump instantly.

Instead it approaches the final value gradually.

Example:

  • tank heating
  • mixing concentration
  • simple RC circuits

Process gain (K_p)

This tells you how much output changes relative to input.

K_p=\frac{\Delta y}{\Delta u}

K_p=\frac{\Delta y}{\Delta u}

If gain is large → small input gives big output change


Time constant (\tau_p)

This is EXTREMELY important.

It tells how fast the system responds.

After 1 time constant:

63.2%

of the total change is completed.

63.2%

This is one of the most famous numbers in control systems.


Key memory points

After:

  • (1\tau) → 63.2%
  • (3\tau) → 95%
  • (4\tau) → 98%

This is VERY exam-relevant.


Step response of first-order system

For a step input:

y(t)=AK_p(1-e^{-t/\tau_p})

y(t)=AK_p\left(1-e^{-t/\tau_p}\right)

This gives the classic exponential rise curve.

This curve is one of the most important in control theory.


3) Impulse response of first-order system

For an impulse:

y(t)=\frac{AK_p}{\tau_p}e^{-t/\tau_p}

y(t)=\frac{AK_p}{\tau_p}e^{-t/\tau_p}

Instead of rising, it starts high and decays exponentially.

This is commonly used in tracer experiments.

The reactor salt example in the chapter is a great real-life application.


4) Ramp response of first-order system

This is VERY important conceptually.

For ramp input, output also becomes ramp-like, but delayed.

The output follows with a lag.

At long times:

y(t)\approx aK_p(t-\tau_p)

y(t)\approx aK_p(t-\tau_p)

Meaning:

the system behaves as if it is “late” by one time constant.

This is a powerful intuition.


5) Second-Order Processes

Now it gets more interesting.

Second-order systems can oscillate.

Equation:

\tau_n^2\frac{d^2y}{dt^2}+2\zeta\tau_n\frac{dy}{dt}+y=K_pu

\tau_n^2\frac{d^2y}{dt^2}+2\zeta\tau_n\frac{dy}{dt}+y=K_pu

Main parameters:

  • (K_p) = gain
  • (\tau_n) = natural period/time scale
  • (\zeta) = damping factor

MOST important: damping factor (\zeta)

This controls the shape of response.


Overdamped ((\zeta >1))

Slow response

No oscillation

Smooth approach


Critically damped ((\zeta=1))

Fastest possible response without oscillation

This is usually desirable.


Underdamped ((\zeta<1))

Oscillatory response

Overshoot + ringing

This is one of the most important concepts in dynamic systems.


6) Important second-order characteristics

These are very exam-relevant.


Rise time

Time required to first reach final value


Overshoot

How much the response exceeds the final value

Example: final = 10 peak = 12

overshoot = 20%


Decay ratio

Ratio of successive oscillation peaks

Shows how quickly oscillations disappear


Settling time

Time until response stays within ±5%

This is used a LOT in controller tuning.


7) Integrating processes

This is extremely important for tank level systems.

Equation:

\rho A_c\frac{dL}{dt}=F_-F_

\rho A_c\frac{dL}{dt}=F_-F_

Key idea:

the output keeps accumulating.

Example:

  • tank filling
  • charge storage
  • position from velocity

Why “integrating”?

Because output is the integral of input.

If inflow > outflow continuously

the level keeps rising forever

This is different from first-order systems which stabilize.

This is a HUGE conceptual difference.


8) High-order processes

These are systems with multiple time constants.

Example: distillation columns

Many trays → many first-order subsystems

Transfer function:

G(s)=\frac{K_p}{(\tau_ps+1)^n}

G(s)=\frac{K_p}{(\tau_ps+1)^n}

As (n) increases:

  • slower response
  • more sluggish
  • looks delayed

9) Deadtime

This is VERY important.

Deadtime means:

input changes now, but output changes later.

Example: temperature sensor far away from reactor

Transport delay

G(s)=e^{-\theta s}

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This is common in industry.

Long pipes sampling delays measurement delays


10) FOPDT model

VERY VERY important.

First Order Plus Dead Time

G(s)=\frac{K_pe^{-\theta_ps}}{\tau_ps+1}

G(s)=\frac{K_pe^{-\theta_ps}}{\tau_ps+1}

This is one of the most used industrial approximations.

Why?

Because real processes often behave like:

  • some delay
  • then smooth exponential response

This model captures both.


BIG picture summary

Think of the models like personalities:

  • first-order → smooth exponential
  • second-order → may oscillate
  • integrating → keeps accumulating
  • high-order → sluggish
  • deadtime → delayed response
  • FOPDT → delayed + smooth

This chapter is basically teaching you the “language” of control engineering.

Once you master these response shapes, later controller tuning becomes much easier.

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