Terminal velocity
Sphere falling through viscous fluid reaches terminal velocity when net force = 0: v_t = (2/9) r² g (ρ_s - ρ_f) / η, where ρ_s, ρ_f are sphere and fluid densities.
-- NCERT, p. 10A sphere dropped into a viscous liquid does not accelerate forever. As it speeds up, the viscous drag force (Stokes' law: F = 6πηrv) grows until it, together with buoyancy, exactly balances the gravitational pull. From that instant onward, the net force is zero and the sphere falls at a constant speed called terminal velocity.
The expression follows directly from setting weight equal to buoyancy plus drag:
v_t = (2r²g(ρ_s − ρ_f)) / (9η)
where r is the sphere radius, ρ_s and ρ_f are the densities of the sphere and fluid, η is the fluid viscosity, and g is the acceleration due to gravity (NCERT Class 11 Physics, Chapter 10 — Mechanical Properties of Fluids, page 10).
The high-frequency trap in this topic: treating terminal velocity as proportional to r (linear) instead of r². Stokes' drag is proportional to r·v, but gravitational minus buoyant force is proportional to r³ (volume). When you balance them, v_t comes out proportional to r². Doubling the radius quadruples the terminal velocity — not doubles it.
Shape of the v–t curve. The sphere starts from rest with maximum acceleration (g_eff). As v increases, drag increases, so acceleration decreases continuously. The curve is concave-down, asymptotically approaching v_t. It is NOT a straight line followed by a flat line — there is no sharp kink.
Watch-out for negative (ρ_s − ρ_f). If the sphere is less dense than the fluid, the "terminal velocity" is upward (the sphere rises). The formula still applies; the direction reverses.
Select an option to see the explanation. Wrong answers show why your choice was tempting — and name the exact trap it exploits.
At terminal velocity, the net force on a sphere falling through a viscous fluid is:
The SI unit of coefficient of viscosity (η) is:
Stokes' law for viscous drag on a sphere is valid when:
A metal sphere of radius r falls through a viscous liquid and reaches terminal velocity v_t. A second sphere of the same material and density but radius 2r falls through the same liquid. Its terminal velocity is:
Two identical spheres fall through two different viscous liquids. Liquid A has viscosity η and liquid B has viscosity 3η. Both liquids have the same density. The ratio of terminal velocities v_A : v_B is:
A sphere of density 2.5 × 10³ kg/m³ falls through a liquid of density 1.5 × 10³ kg/m³. If the liquid density were changed to 2.0 × 10³ kg/m³ (same viscosity, same sphere), the terminal velocity would become:
A sphere is released from rest in a viscous liquid. Which of the following best describes the velocity–time graph?
A sphere of radius 1.0 × 10⁻³ m and density 8.0 × 10³ kg/m³ falls through oil of density 1.0 × 10³ kg/m³ and viscosity 9.8 Pa·s. Taking g = 9.8 m/s² (exact for this problem), the terminal velocity is approximately:
Pattern: Terminal velocity scaling (based on PYQ pattern NEET pattern: terminal velocity scaling — observed in NEET 2021, 2022)
Given
A steel ball of radius r₁ = 2.0 × 10⁻³ m reaches terminal velocity v₁ = 4.0 × 10⁻² m/s in a viscous liquid. A second steel ball of radius r₂ = 4.0 × 10⁻³ m is dropped into the same liquid.
Required
Terminal velocity v₂ of the second ball.
Concept
Terminal velocity is proportional to r² (from v_t = (2r²g(ρ_s − ρ_f))/(9η)). When the material (ρ_s), fluid (ρ_f, η), and g are all the same, the ratio v₂/v₁ = (r₂/r₁)².
Formula
v₂ = v₁ × (r₂/r₁)²
Substitution
v₂ = 4.0 × 10⁻² × (4.0 × 10⁻³ / 2.0 × 10⁻³)²
Calculation
r₂/r₁ = 2.0 (exact ratio — both radii are given to 2 significant figures, and the ratio is a counting number) (r₂/r₁)² = 4.0 v₂ = 4.0 × 10⁻² × 4.0 = 16 × 10⁻² = 1.6 × 10⁻¹ m/s
Final answer
v₂ = 1.6 × 10⁻¹ m/s (= 0.16 m/s), reported to 2 significant figures matching the given data. The ratio 2.0 is exact (problem-defined integer ratio) and does not limit significant figures.
Common trap
Treating v_t as proportional to r (linear) gives v₂ = 2 × 4.0 × 10⁻² = 8.0 × 10⁻² m/s — exactly half the correct answer. This is the most common wrong-option pattern for terminal velocity scaling questions.
Similar NEET-style question
A raindrop of radius R falls at terminal velocity V through air. If a second raindrop has radius 3R (same density, same air conditions), what is its terminal velocity? *Answer: v_t ∝ r², so the new terminal velocity = V × (3R/R)² = 9V.* ---
Sphere falling through viscous fluid reaches terminal velocity when net force = 0: v_t = (2/9) r² g (ρ_s - ρ_f) / η, where ρ_s, ρ_f are sphere and fluid densities.
-- NCERT, p. 10Conservation of energy along a streamline of incompressible non-viscous flow.
| Symbol | Quantity | SI Unit |
|---|---|---|
| P | pressure | Pa |
| rho | density | kg/m^3 |
| v | speed | m/s |
| g | gravity | m/s^2 |
| h | height | m |
Resistance of a material to uniform compression. Inverse: compressibility.
| Symbol | Quantity | SI Unit |
|---|---|---|
| K | bulk modulus | Pa |
| V | volume | m^3 |
| P | pressure | Pa |
Height a liquid rises (or falls) in a capillary tube. cos(theta) > 0: rises (wetting); < 0: depresses.
| Symbol | Quantity | SI Unit |
|---|---|---|
| h | capillary height | m |
| T | surface tension | N/m |
| theta | contact angle | rad |
| rho | density | kg/m^3 |
| r | tube radius | m |
Pressure at depth h below free surface of fluid of density rho.
| Symbol | Quantity | SI Unit |
|---|---|---|
| P | total pressure | Pa |
| P0 | atmospheric/surface pressure | Pa |
| rho | density | kg/m^3 |
| h | depth | m |
Heat absorbed/released during phase change at constant T. L_fusion or L_vaporisation.
| Symbol | Quantity | SI Unit |
|---|---|---|
| Q | heat | J |
| m | mass | kg |
| L | latent heat | J/kg |
Heat required to raise mass m by temperature Delta_T. Specific heat c is material property.
| Symbol | Quantity | SI Unit |
|---|---|---|
| Q | heat | J |
| m | mass | kg |
| c | specific heat | J/kg/K |
| Delta_T | temp change | K |
Radiation power from a body. Black body epsilon=1; net to surroundings P = sigma*epsilon*A*(T^4 - T_s^4).
| Symbol | Quantity | SI Unit |
|---|---|---|
| sigma | Stefan-Boltzmann = 5.67e-8 | W/m^2/K^4 |
| epsilon | emissivity (0-1) | - |
| A | surface area | m^2 |
| T | absolute temp | K |
Drag force on a sphere of radius r moving with velocity v through viscous fluid (low Reynolds number).
| Symbol | Quantity | SI Unit |
|---|---|---|
| F | drag force | N |
| eta | viscosity | Pa*s |
| r | sphere radius | m |
| v | velocity | m/s |
Excess internal pressure due to surface tension. Bubble has 2 surfaces, hence factor 4.
| Symbol | Quantity | SI Unit |
|---|---|---|
| Delta_P | excess pressure | Pa |
| T | surface tension | N/m |
| r | radius | m |
Constant velocity reached when net force is zero (gravity balanced by buoyancy + viscous drag).
| Symbol | Quantity | SI Unit |
|---|---|---|
| v_t | terminal velocity | m/s |
| r | sphere radius | m |
| rho_s | sphere density | kg/m^3 |
| rho_f | fluid density | kg/m^3 |
| eta | viscosity | Pa*s |
Fractional change in length, area, volume per degree temperature change.
| Symbol | Quantity | SI Unit |
|---|---|---|
| alpha | linear coefficient | 1/K |
| beta | volume coefficient | 1/K |
| Delta_T | temperature change | K |
Ratio of longitudinal stress to longitudinal strain in a stretched wire/rod within elastic limit.
| Symbol | Quantity | SI Unit |
|---|---|---|
| Y | Young's modulus | Pa |
| F | applied force | N |
| A | cross-section area | m^2 |
| L | original length | m |
| Delta_L | extension | m |
These are the exact patterns that cause wrong answers in NEET. Each trap includes when it triggers and how to avoid it.
Category: Similar Terms
Student uses 2T/r for soap bubble (drop formula). Bubble has 2 surfaces → 4T/r.
Question mentions soap bubble OR liquid drop OR air bubble in liquid.
Drop in air: 1 surface → 2T/r. Soap bubble in air: 2 surfaces → 4T/r. Air bubble in liquid: 1 surface → 2T/r.
Category: Similar Terms
Student uses Y formula when problem is about volumetric compression (use K) or vice versa.
Problem describes longitudinal stretching (use Y), volumetric pressure (use K), or shear (use G).
Y: longitudinal stress/strain. K: volumetric. G: shear. Match modulus to deformation type.
Root cause: concept gap
Drop in air: 1 surface → ΔP = 2T/r. Soap bubble: 2 surfaces (inner + outer) → ΔP = 4T/r. Air bubble inside liquid: 1 surface → 2T/r.
Root cause: formula misuse
v_t ∝ r² (because Stokes drag ∝ r v, gravity ∝ r³ - r³ = r³_diff). Doubling radius quadruples terminal velocity, not doubles.
Root cause: formula misuse
Y for longitudinal stretch (FL/A·ΔL); K for volumetric compression (-V·dP/dV); G for shear. Match modulus type to deformation type before computing.
If a soap bubble expands, the pressure inside the bubble
forgets height term
Drops rho*g*h term
equates pressures incorrectly
Picks wrong reference points
ignores mass difference
Compares only specific heats, not masses
uses 2T r instead of 4T r for bubble
Treats soap bubble like a drop
expects linear acceleration
Default to constant acceleration without recognising drag-induced terminal v
uses bulk modulus formula
Confuses Y with K
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