Mechanical Properties of Fluids
Pascal's law, hydraulic lift, hydrostatic pressure, barometer, continuity, Bernoulli's theorem, viscosity & surface tension.
Topic 9.2.1: Pascal's Law & Hydraulic Lift / Brakes
1500 kg SUV smoothly into the air! How can a finger-sized push lift an elephant-sized car? Not by creating free energy — by trapping incompressible oil inside connected pistons under Pascal's Law!P = F_normalA | SCALAR! | SI unit: Pa = N/m²F₁A₁ = F₂A₂ ⇒ F₂ = F₁ (A₂A₁) = F₁ (r₂r₁)²F₂ grows by A₂/A₁, while stroke shrinks by A₁/A₂ so F₁d₁ = F₂d₂!10 Pa, and EVERY square centimetre of the bottle walls suddenly feels an extra 10 Pa push! Put a wide 100 cm² lid on the other side, and those 100 little pushes team up to lift 100× more weight!- 1Pressure is a Scalar: Even though force is a vector, fluid pressure at a point pushes perpendicular to ANY surface placed there with the same magnitude — so
Phas no fixed direction. - 2Same-Height Rule & Transmission: In a fluid at rest, pressure is equal at all points at the same horizontal level, and any added pressure
ΔPspreads equally throughout the closed vessel. - 3Hydraulic Brakes & Lifts: Pressing the brake pedal pushes master-cylinder fluid (small
A₁) to wide wheel cylinders (largeA₂), gripping all four tyres equally at once!
P = F₁A₁ = F₂A₂ | Volume pushed: A₁ d₁ = A₂ d₂ ⇒ Work: F₁ d₁ = F₂ d₂
2 cm and 20 cm. To lift a 1500 kg car (F₂ ≈ 15,000 N):A₂A₁ = (202)² = 10² = 100.Required push
F₁ = 15,000 / 100 = 150 N (just 15 kg weight)! To lift the car 10 cm, push the small piston 100 × 10 cm = 10 m!
F/A!). Second, a hydraulic lift does NOT violate energy conservation — it multiplies force, while the small piston must travel proportionally farther so Work_in = Work_out!Topic 9.2.2 – 9.2.3: Pressure with Depth, Manometer & Torricelli Barometer
P = P_a + ρ g h | Gauge Pressure: P_g = P − P_a = ρ g h1 atm = 1.013 × 10⁵ Pa = 76 cm Hg ≈ 10.3 m water | 1 bar = 10⁵ Pah & density ρ — NOT container shape!1 atm = 10.3 m (3-storey building!), Mercury (13.6× denser!) = just 0.76 m (76 cm) — that's why barometers use Mercury!h and area A pressing down from above: its weight is mg = (ρ A h) g. Divide by A, add air pressing on the top surface (P_a), and boom — total pressure at depth h is P = P_a + ρ g h!- 1Hydrostatic Paradox: Pour water to the exact same height
hinside a wide funnel, a zig-zag pipe, and a narrow straw. Bottom pressureP_a + ρghis identical in all three because tilted walls push sideways/upward to carry extra fluid weight! - 2Torricelli's Mercury Barometer: Air pressure outside pushes mercury up an evacuated glass tube to height
h = 76 cm:P_a = ρ_Hg g h = 13600 × 9.8 × 0.76 ≈ 1.013 × 10⁵ Pa. (Also1 torr = 1 mm Hg ≈ 133 Pa.) - 3Open-Tube Manometer: Measures gauge pressure
P − P_a = ρ g hfrom the U-tube liquid level differenceh(used in blood pressure cuffs and gas cylinders!).
P = P_a + ρ g h | Gauge: P_g = ρ g h | Buoyancy (Archimedes): F_B = V_sub ρ_fluid g
20 m depth in a lake (ρ = 1000 kg/m³, g = 10 m/s², P_a = 10⁵ Pa):• Gauge pressure =
1000 × 10 × 20 = 2 × 10⁵ Pa (2 atm).• Total (Absolute) pressure =
10⁵ + 2 × 10⁵ = 3 × 10⁵ Pa (3 atm)!
P − P_a), NOT absolute pressure! (2) Even if you tilt a mercury barometer tube slightly or use a wider tube, the vertical height h = 76 cm stays unchanged (slant length grows, vertical height does not)! (3) Dam walls are made thick at the bottom because pressure ρgh increases linearly with depth!Topic 9.3: Streamline Flow & Equation of Continuity
A₁ v₁ = A₂ v₂ = constant (Volume flow rate Q = A v)v ∝ 1/A ∝ 1/d²)! Halving pipe diameter makes water sprint 4× FASTER!A₁) entering a narrow classroom doorway (A₂). If nobody piles up inside (incompressible fluid!), everyone MUST walk much faster (v₂) through the narrow door so the same number of kids pass every second!- 1Steady vs Turbulent Flow: At low speeds fluid layers glide smoothly along fixed curves called streamlines (tangent = velocity at that point). Above a critical speed, eddies swirl chaotically (turbulent flow, like fast rapids or smoke curling up!).
- 2Mass Conservation Derivation: In time
Δt, mass entering areaA₁isρ A₁ v₁ Δt, and mass exiting areaA₂isρ A₂ v₂ Δt. For an incompressible liquid (ρconstant),A₁ v₁ = A₂ v₂! - 3Streamline Spacing Rule: Closely packed streamlines mean high speed; wide-spaced streamlines mean low speed!
A₁ v₁ = A₂ v₂ ⇒ Circular pipe: π r₁² v₁ = π r₂² v₂ ⇒ v₂ = v₁ (d₁d₂)²
1.5 m/s through a 2 cm diameter pipe that narrows to a 1 cm nozzle.Since diameter halved (
d₁/d₂ = 2), speed becomes v₂ = 1.5 × 2² = 1.5 × 4 = 6.0 m/s!
Av = const) expresses Conservation of Mass (for incompressible fluids).Topic 9.4: Bernoulli's Principle, Venturi Meter, Efflux & Aerofoil Lift
P + 12 ρ v² + ρ g h = constant (Energy per unit volume!)h₁ = h₂): where speed v is HIGH, pressure P is LOW!h below surface: speed v = √(2gh)! Max range at h = H/2!P) + Kinetic (½ρv²) + Potential (ρgh) = Constant!- 1Venturi Meter: Narrows a pipe from area
A₁to throatA₂. By continuityv₂ > v₁, so Bernoulli makes throat pressure drop (P₁ − P₂ = ½ ρ (v₂² − v₁²)), measured cleanly by a U-tube manometer to calculate pipe speed! - 2Torricelli's Law (Speed of Efflux): Water shooting from a small tank hole at depth
hbelow the free surface has speedv = √(2gh)— identical to a stone dropped freely through heighth! - 3Dynamic Lift (Aerofoil & Magnus Effect): Curved airplane wings speed up air on top (low
P) relative to bottom (highP) → net upward lift! A spinning cricket/football drags air faster on one side → Magnus swing!
P₁ + ½ρv₁² + ρgh₁ = P₂ + ½ρv₂² + ρgh₂ | Efflux: v = √(2gh), Range: R = 2√(h(H−h))
2 m/s to 6 m/s (ρ = 1000 kg/m³). Find the pressure drop:P₁ − P₂ = ½ ρ (v₂² − v₁²) = ½ × 1000 × (36 − 4) = 500 × 32 = 16,000 Pa!
v = √(2gh), h is depth below the open top surface, NOT height from the floor! (3) Why is blood flow through narrowed arteries dangerous (heart attack risk)? High blood speed inside constricted plaque lowers internal pressure, letting external pressure collapse the artery temporarily!Topic 9.5: Viscosity, Stokes' Law & Terminal Velocity
η = F / Av / l | SI: Pa·s (1 poise = 0.1 Pa·s)F_v = 6 π η a v (Viscous drag on sphere of radius a at speed v!)v_t = 2 a² (ρ − σ) g9 η (ρ = sphere, σ = fluid; v_t ∝ a²!)η_liquid ↓) and Gases STICKIER (η_gas ↑)! Warm coconut oil pours fast; hot air resists more!v = 0), top layer moves fastest, and honey molecules tug hard between layers! When a steel ball drops into oil, viscous drag grows with speed until Upward (Drag + Buoyancy) = Downward Weight — then acceleration stops and it glides at steady terminal velocity v_t!- 1Coefficient of Viscosity (
η): Ratio of shearing stress (F/A) to velocity gradient (dv/dx). SI unit:poiseuille (Pl) = N·s/m² = Pa·s; CGS unit:poise(1 Pl = 10 poise). - 2Stokes' Law: A small smooth sphere of radius
amoving at velocityvexperiences viscous dragF_v = 6 π η a vopposite to motion. - 3Terminal Velocity Derivation: At equilibrium:
6 π η a v_t + 43πa³ σ g = 43πa³ ρ g⇒v_t = 2 a² (ρ − σ) g9 η!
F = 6 π η a v | v_t = 2 a² (ρ − σ) g9 η | [η] = [M L⁻¹ T⁻¹]
1 : 2 falling through air. Find the ratio of their terminal velocities:Since
v_t ∝ a², doubling radius quadruples terminal speed: v₁ : v₂ = 1² : 2² = 1 : 4! (That is why tiny mist droplets practically float!)
η in liquids (weakening cohesion) but INCREASES η in gases (faster random molecular collisions across layers)! Second, if fluid density σ > sphere density ρ (like an air bubble inside water!), v_t flips negative — the bubble shoots UPWARD!Topic 9.6: Surface Tension, Excess Pressure in Drops & Capillary Rise
S = Fl = Surface EnergyΔA | SI: N/m or J/m²2SR | Soap bubble (2 surfaces!): 4SRh = 2S cos θr ρ g (θ < 90° rises; Mercury θ > 90° depresses!)2S/R; Soap bubble = 2 skins (inside + outside) = 4S/R! Smaller bubble has BIGGER pressure (1/R)!- 1Surface Energy Work: Increasing liquid surface area by
ΔAcosts workW = S ΔA(for a soap film with two faces, useW = 2 S ΔA!). Adding soap lowers water's surface tensionSso clothes clean easily! - 2Angle of Contact (
θ): Angle inside the liquid between tangent and solid wall. Water–clean glass has acuteθ(concave meniscus, wets glass,cos θ > 0). Mercury–glass has obtuseθ ≈ 140°(convex meniscus, doesn't wet,cos θ < 0!). - 3Capillary Rise (Jurin's Law): Concave meniscus has lower pressure just below it by
2S cos θ / r, pulling liquid up heighth = 2S cos θ / (r ρ g)(noticeh ∝ 1/r: thinner straw = higher climb!).
ΔP = 2SR | Soap Bubble: ΔP = 4SR | Capillary: h = 2S cos θr ρ g
S = 0.073 N/m, θ ≈ 0°, ρ = 1000 kg/m³) enters a capillary tube of radius r = 0.5 mm = 5 × 10⁻⁴ m (g = 9.8 m/s²).Rise
h = 2 × 0.073 × 1(5 × 10⁻⁴) × 1000 × 9.8 = 0.1464.9 ≈ 0.0298 m ≈ 3.0 cm!
ΔP = 4S/R ∝ 1/R, the SMALLER bubble has HIGHER internal pressure, so air rushes from SMALL to LARGE (small shrinks, large swells)! (2) A soap film/bubble has TWO free surfaces, so always use 4S/R for excess pressure and 2ΔA for surface energy!Solved Previous Year Questions (Kerala DHSE & NCERT)
Q1 (Kerala HSE March • 2 Marks): State Pascal's law for transmission of fluid pressure. Explain how a hydraulic lift multiplies force without violating conservation of energy.
In a hydraulic lift,
F₂ = F₁ (A₂/A₁) multiplies force when A₂ > A₁. However, fluid volume displaced is equal (A₁ d₁ = A₂ d₂), so input work F₁ d₁ equals output work F₂ d₂ — energy is conserved.Q2 (Kerala HSE Model • 1 Marks): Three vessels of different shapes (wide, narrow, slanted) have the same base area and are filled with water to the exact same height h. Compare the pressure and force on their bases.
P = P_a + ρgh depends solely on vertical height h and density ρ, and since base area A is identical, force P × A is also identical.Q3 (Kerala HSE March • 3 Marks): State Bernoulli's principle and write its mathematical expression. Mention two essential assumptions and two practical applications.
P + ½ρv² + ρgh = constant.Assumptions: Fluid is incompressible, non-viscous (zero friction), and flow is steady/irrotational.
Applications: Venturi meter (flow speed measurement), dynamic aerofoil lift on aircraft wings, Magnus swing of spinning balls, and roof lift-off in storms.
Q4 (Kerala HSE Say • 2 Marks): What is Torricelli's law of speed of efflux? At what depth should a hole be made in a tank of total height H for maximum horizontal range?
h below the free surface is v = √(2gh) (equal to free-fall speed from height h).Horizontal range
R = 2√(h(H − h)) is maximum when h = H / 2 (halfway up the tank), giving R_max = H.Q5 (Kerala HSE March • 3 Marks): State Stokes' law and derive the expression for terminal velocity v_t of a sphere of radius a and density ρ falling through a fluid of density σ and viscosity η.
v is F_v = 6 π η a v.At terminal velocity
v_t, net downward force is zero: Weight = Buoyancy + Viscous Drag.(4/3)πa³ ρ g = (4/3)πa³ σ g + 6 π η a v_t6 π η a v_t = (4/3)πa³ (ρ − σ) g ⇒ v_t = 2 a² (ρ − σ) g / (9 η).Q6 (Kerala HSE March • 2 Marks): Why is excess pressure inside a soap bubble twice that inside a liquid drop of the same radius R?
ΔP_drop = 2S / R.A soap bubble has two free surfaces (inner wall and outer wall in contact with air), doubling the surface tension inward pull to
ΔP_bubble = 4S / R.Q7 (Kerala HSE Say • 3 Marks): Derive the expression for capillary rise h of a liquid of surface tension S, density ρ, and contact angle θ inside a tube of radius r.
R = r / cos θ.Pressure just below the meniscus is lower than atmospheric pressure
P₀ by ΔP = 2S / R = 2S cos θ / r.At equilibrium, liquid column of height
h balances this deficit: h ρ g = 2S cos θ / r.Hence
h = 2S cos θ / (r ρ g).Q8 (NCERT / DHSE Model • 2 Marks): Calculate the terminal velocity of an air bubble of radius 0.5 mm rising in water (viscosity η = 1.0 × 10⁻³ Pa·s, ρ_water = 1000 kg/m³, g = 9.8 m/s², neglect air density).
a = 0.5 × 10⁻³ m, ρ_bubble ≈ 0, σ_water = 1000 kg/m³.Magnitude:
|v_t| = 2 a² (σ − ρ) g / (9 η) = [2 × (0.5 × 10⁻³)² × 1000 × 9.8] / (9 × 10⁻³)=
[2 × 2.5×10⁻⁷ × 9800] / (9 × 10⁻³) = 4.9×10⁻³ / (9×10⁻³) ≈ 0.54 m/s (directed upward!).