Concept Core
Elasticity, viscosity, and surface tension β the three pillars of properties of matter.
Elasticity β Stress, Strain, and Young's Modulus
Stress = Force / Area (N/mΒ²)
Strain = Change in dimension / Original dimension (dimensionless)
Young's Modulus Y = Tensile Stress / Tensile Strain = FL/(AΞL)
Bulk Modulus K = Pressure / Volumetric Strain = βP/(ΞV/V)
Modulus of Rigidity Ξ· = Shear Stress / Shear Strain
Hooke's Law: Stress β Strain (within elastic limit). Beyond elastic limit β permanent deformation.
Elastic Energy Stored in a Wire
Energy U = Β½ Γ Stress Γ Strain Γ Volume
U = Β½ Γ F Γ ΞL (since F = YΒ·AΒ·ΞL/L)
Energy density = Β½ Γ Stress Γ Strain = StressΒ²/(2Y)
Viscosity β Stokes' Law
Viscous force (Stokes): F = 6ΟΞ·rv
Terminal velocity: vβ = 2rΒ²(ΟβΟ)g / (9Ξ·)
Poiseuille's Law: Q = Οrβ΄ΞP/(8Ξ·L) (flow through pipe)
Ξ· = coefficient of viscosity (NΒ·s/mΒ²). Terminal velocity when weight = buoyancy + viscous drag. For liquids, Ξ· decreases with temperature. For gases, Ξ· increases with temperature.
Surface Tension
Surface tension T = Force / Length (N/m)
Excess pressure inside bubble: ΞP = 4T/r (soap bubble, 2 surfaces)
Excess pressure inside drop: ΞP = 2T/r (one surface)
Capillary rise: h = 2T cosΞΈ/(Οgr)
Soap bubble has 2 surfaces (inner and outer), hence 4T/r. Liquid drop has 1 surface, hence 2T/r.
Bernoulli's Equation & Continuity
Continuity: Aβvβ = Aβvβ (incompressible fluid)
Bernoulli: P + Β½ΟvΒ² + Οgh = constant
Torricelli: v = β(2gh) (efflux from a hole)
Thermal Expansion
Linear: ΞL = Ξ±LΞT β L = Lβ(1+Ξ±ΞT)
Area: ΞA = 2Ξ±AΞT (Ξ² = 2Ξ±)
Volume: ΞV = 3Ξ±VΞT (Ξ³ = 3Ξ±)
Relation: Ξ± : Ξ² : Ξ³ = 1 : 2 : 3
Formula Vault
Properties of matter formulas for EAPCET.
Young's Modulus
Y = FL/(AΞL)
F = force; L = length; A = area
Bulk Modulus
K = βPV/ΞV
Resistance to compression
Elastic Energy
U = Β½ Γ F Γ ΞL = Β½ Γ Stress Γ Strain Γ V
V = volume of wire
Stokes' Law
F = 6ΟΞ·rv
Ξ· = viscosity; r = radius; v = speed
Terminal Velocity
vβ = 2rΒ²(ΟβΟ)g/(9Ξ·)
Ο = sphere density; Ο = fluid density
Surface Tension
T = F/l (N/m)
F = force along length l
Excess P in Soap Bubble
ΞP = 4T/r
Two surfaces β factor 4
Excess P in Drop
ΞP = 2T/r
One surface β factor 2
Capillary Rise
h = 2T cosΞΈ/(Οgr)
ΞΈ = contact angle; r = tube radius
Thermal Expansion
Ξ±:Ξ²:Ξ³ = 1:2:3
Linear, area, volume coefficients
Worked Examples
5 problems β Young's modulus, terminal velocity, surface tension, Bernoulli, and a trap.
EasyFind extension of wire: Y=2Γ10ΒΉΒΉ Pa, L=1m, A=10β»βΆmΒ², F=200NβΎ
A steel wire (Y = 2Γ10ΒΉΒΉ N/mΒ², L = 1 m, A = 10β»βΆ mΒ²) is loaded with F = 200 N. Find the extension.
1
Y = FL/(AΞL) β ΞL = FL/(YA)
2
ΞL = 200 Γ 1/(2Γ10ΒΉΒΉ Γ 10β»βΆ) = 200/(2Γ10β΅) = 10β»Β³ m = 1 mm
β Extension = 1 mm
EasyFind excess pressure inside a soap bubble of radius 5cm (T=0.03 N/m)βΎ
Find the excess pressure inside a soap bubble of radius 5 cm. Surface tension = 0.03 N/m.
1
Soap bubble (2 surfaces): ΞP = 4T/r = 4 Γ 0.03/(0.05) = 0.12/0.05 = 2.4 Pa
β Excess pressure = 2.4 Pa
MediumFind terminal velocity of sphere: r=0.5mm, Ο=8000 kg/mΒ³, Ο=1000 kg/mΒ³, Ξ·=0.1 PaΒ·sβΎ
Find terminal velocity of a steel sphere (r = 0.5 mm, Ο = 8000 kg/mΒ³) falling through oil (Ο = 1000 kg/mΒ³, Ξ· = 0.1 PaΒ·s). g = 10 m/sΒ².
1
vβ = 2rΒ²(ΟβΟ)g/(9Ξ·)
2
= 2Γ(0.5Γ10β»Β³)Β²Γ(8000β1000)Γ10/(9Γ0.1)
3
= 2Γ2.5Γ10β»β·Γ70000/0.9 = 3.5Γ10β»Β²/0.9 β 0.039 m/s β 3.9 cm/s
β Terminal velocity β 3.9 cm/s
EAPCET LevelWater flows from radius 4cm pipe into radius 2cm pipe β find speed ratioβΎ
Water flows from a pipe of radius 4 cm into one of radius 2 cm. Find the ratio of speeds.
1
Continuity equation: Aβvβ = Aβvβ
2
Ο(4)Β²vβ = Ο(2)Β²vβ
3
16vβ = 4vβ β vβ/vβ = 4
4
The smaller pipe has 4Γ higher speed.
β vβ : vβ = 4 : 1
Trap QuestionSoap bubble vs liquid drop β same formula for excess pressure?βΎ
A soap bubble and a liquid drop both have radius r = 2 cm, surface tension T = 0.04 N/m. Compare their excess pressures.
1
The trap: Same formula doesn't apply to both.
2
Soap bubble: 2 surfaces (inner and outer). ΞP = 4T/r = 4Γ0.04/0.02 = 8 Pa
3
Liquid drop: 1 surface (the outer surface only). ΞP = 2T/r = 2Γ0.04/0.02 = 4 Pa
4
Soap bubble has exactly double the excess pressure of a liquid drop of the same radius and surface tension.
β Soap bubble: 8 Pa; Drop: 4 Pa β bubble is double (two surfaces vs one)
Mistake DNA
3 properties of matter errors from EAPCET distractor analysis.
π«§
Using 2T/r for Soap Bubble (Should Be 4T/r)
A soap bubble has TWO surfaces (inner and outer), so the pressure formula is 4T/r, not 2T/r.
β Wrong
Soap bubble ΞP = 2T/r β
(one-surface formula;
only valid for drop)
β Correct
Soap bubble: 4T/r β
(two surfaces contribute)
Liquid drop: 2T/r β
(only outer surface)
Remember: soap film has inner and outer surfaces. Each contributes 2T/r. Total = 4T/r. A liquid drop has only one curved surface: ΞP = 2T/r.
π‘οΈ
Ξ· of Liquids Increases with Temperature (Like Gases)
For liquids, viscosity DECREASES with temperature (molecules have more KE, layers slide more easily). For gases, Ξ· INCREASES with temperature.
β Wrong
Heating oil β more
viscous (Ξ· increases) β
(that's for gases!)
β Correct
Liquids: Ξ· decreases with T β
(honey flows easier when warm)
Gases: Ξ· increases with T β
(more molecular collisions)
Physical intuition: in liquids, viscosity arises from molecular attraction. Higher T β molecules overcome attraction β Ξ· decreases. In gases, viscosity arises from molecular momentum transfer between layers, which increases with T.
π
Ξ±:Ξ²:Ξ³ = 1:2:3 Means Ξ² = 2 and Ξ³ = 3
The ratio is Ξ±:Ξ²:Ξ³ = 1:2:3, meaning Ξ² = 2Ξ± and Ξ³ = 3Ξ±. Not Ξ² = 2 and Ξ³ = 3 in absolute terms.
β Wrong
Ξ± = 12Γ10β»βΆ/Β°C β
Ξ² = 2, Ξ³ = 3 β
(should be 2Ξ±, 3Ξ±)
β Correct
Ξ² = 2Ξ± = 24Γ10β»βΆ/Β°C β
Ξ³ = 3Ξ± = 36Γ10β»βΆ/Β°C β
The ratio is preserved
not the absolute value
The thermal expansion coefficients maintain ratio 1:2:3 always. If linear expansion is Ξ±, area expansion is 2Ξ± and volume expansion is 3Ξ±.
Chapter Intelligence
Properties of matter integrates with fluids, thermal physics, and elasticity.
EAPCET Weightage (2019β2024)
Surface tension (bubbles, drops, capillary)~7 Young's modulus and stress/strain~6 Viscosity and terminal velocity~5 Thermal expansion Ξ±:Ξ²:Ξ³~3
High-Yield PYQ Patterns
Excess pressure in soap bubble vs dropTerminal velocity calculationYoung's modulus extension of wireBernoulli: speed ratio in pipesCapillary rise heightΞ±:Ξ²:Ξ³ = 1:2:3 propertyElastic energy in stretched wire
Exam Strategy
- Soap bubble (2T/r each surface): ΞP = 4T/r. Liquid drop (1 surface): ΞP = 2T/r. The factor-of-2 difference is tested directly every few years.
- Terminal velocity: all factors in the formula vβ = 2rΒ²(ΟβΟ)g/(9Ξ·). Key insight: vβ β rΒ² β doubling radius β 4Γ terminal velocity.
- Thermal expansion: Ξ³ = 3Ξ± always. This is a direct fact question. Volume expands 3Γ more than linear for same ΞT.
- Continuity equation: Aβvβ = Aβvβ. Narrower pipe β faster flow. This is the basis of the Venturi meter and atomiser.