Quick revisionFluids I + II on one pageEach idea in one line, its formula, the trap and how NEET asks it Class 11 · Chapter 9 · Part 2

Viscosity & Surface Tension

Why honey pours slowly, why raindrops don't hit like bullets, why drops are round and why water climbs up a thin tube. This is the second half of Mechanical Properties of Fluids, built up from zero to exam level.

CUT-6 syllabus: up to 9.6.5 Test-06 traps marked 11 interactive simulations

Pressure, Pascal's law, buoyancy, continuity and Bernoulli are on Fluids I. Short on time? Read the formula cards, the red “Exam trap” boxes and the night-before checklist.

9.5 BasicsCore

Viscosity: friction inside a fluid

Tip a jar of honey and a glass of water. Both are liquids, yet honey crawls and water rushes out. Stir both with a spoon: honey drags the spoon back far more. The property that makes the difference is viscosity.

Picture a flowing liquid as a stack of very thin sheets (layers) sliding over one another, like the pages of a book when you push the top cover sideways. The layer touching a solid surface sticks to it and does not move. Each layer above moves a little faster than the one below. Neighbouring layers rub against each other: the faster layer tries to drag the slower one forward, and the slower one tries to hold the faster one back. This internal friction between layers is viscosity.

This orderly layer-by-layer flow is called laminar (streamline) flow. Flow through a pipe is also laminar at low speed: the layer at the wall is at rest and the central layer is fastest.

Definition

Viscosity is the property of a fluid by which it opposes relative motion between its adjacent layers. The tangential force between layers is the viscous force. A fluid with zero viscosity (and incompressible) is called an ideal fluid.

Newton found experimentally that the viscous force \(F\) between two layers is proportional to the area of contact \(A\) and to how quickly the speed changes as you move from one layer to the next: the velocity gradient \(dv/dx\), where \(x\) is measured perpendicular to the flow.

Newton's law of viscosity
\[ F = -\,\eta A \frac{dv}{dx} \]
\(\eta\) (eta) = coefficient of viscosity. The minus sign says the force opposes the relative motion. For a liquid film of thickness \(d\) under a plate moving at \(v\): \(F = \eta A v/d\).
Symbols and assumptions: F = signed viscous force (N), opposing relative layer motion; η = dynamic viscosity (Pa·s); A = sheared area (m²); v = flow velocity (m/s); x = distance across layers (m); dv/dx = velocity gradient (s⁻¹). Use |F| = ηA|dv/dx| for the magnitude.
Velocity gradient
\[ \frac{dv}{dx} = \frac{v}{d} \;\;(\text{uniform film}) \]
Change in speed per unit distance across the layers. Unit s⁻¹. It is also the rate of shear strain.
Symbols and assumptions: v = moving-plate speed relative to the fixed plate (m/s); d = film thickness (m); x = perpendicular distance through the film (m); dv/dx = velocity gradient (s⁻¹). The v/d form assumes a linear velocity profile and no slip.
Units & dimensions of η
\[ \eta = \frac{F/A}{v/d} \;\Rightarrow\; [\mathrm{M\,L^{-1}\,T^{-1}}] \]
SI: N s m⁻² = Pa·s (also called poiseuille, PI). CGS: poise. 1 poise = 0.1 Pa·s (so 1 Pa·s = 10 poise).
Symbols and assumptions: η = viscosity (Pa·s); F = viscous-force magnitude (N); A = plate area (m²); v = relative plate speed (m/s); d = film thickness (m). M, L and T in the dimensional expression mean mass, length and time.
Link to Solids

In a solid, shear modulus = shear stress / shear strain. In a fluid, viscosity = shear stress / rate of shear strain. A fluid keeps deforming as long as the force acts, so the rate, not the strain, is what matters. (See shear modulus.)

Interactive

Layers sliding over each other

Velocity gradient–
Viscous stress–
Viscous force F–

Watch the purple dye line: it starts vertical and leans over, because higher layers move faster. Halve d and the gradient (and F) doubles.

Temperature and viscosity: the classic trap

Liquids: viscosity comes mainly from the attraction (cohesion) between neighbouring molecules. Heat a liquid and the molecules move apart and gain energy, so \(\eta\) decreases. Warm honey or engine oil flows easily.

Gases: molecules are far apart; viscosity comes from molecules darting between layers and carrying momentum with them. Hotter means faster molecules and more momentum transfer, so \(\eta\) increases with temperature.

FluidTemperatureη (approx.)
Water20 °C1.0 × 10⁻³ Pa·s
Water100 °C0.3 × 10⁻³ Pa·s (falls)
Blood37 °C≈ 3 × 10⁻³ Pa·s
Castor oil / glycerine20 °C≈ 1 Pa·s
Air20 °C → 100 °C1.8 → 2.2 × 10⁻⁵ Pa·s (rises)
Exam trap · your Q12, Q23, Q42, Q43
  • Gas viscosity increases with temperature. “Viscosity of gases decreases with temperature” is the incorrect statement (Q12). Liquids decrease, gases increase.
  • Ideal fluid: η = 0 (non-viscous) and incompressible (Q42). Not “η = 1”, not “infinite”.
  • For this test, choose a lubricant with sufficiently high viscosity (Q43; you chose low). A viscous oil film is not easily squeezed out from between moving parts, so the metal surfaces stay apart. An oil that is too thin may fail to maintain the film. In practice, viscosity must suit the load, speed and temperature; excessively viscous oil also increases resistance.
  • Viscosity is a property of liquids and gases; solids do not have it.
Where you meet it

Blood viscosity sets how hard the heart must pump; thicker blood means more work. Engine oil grades are viscosity grades. Shock absorbers and door closers use viscous oil to slow motion smoothly.

Worked example · Numerical (like Q36)

A metal plate of area 200 cm² rests on a 2 mm thick layer of glycerine (η = 8.5 poise) spread on a fixed table. What horizontal force keeps it moving at a steady 4 cm/s? (Set the simulation to these values to check.)

Show solution
  1. Convert to SI: A = 200 × 10⁻⁴ = 0.02 m², d = 2 × 10⁻³ m, v = 0.04 m/s, η = 8.5 poise = 0.85 Pa·s.
  2. Steady speed, so the applied force equals the viscous force: \(F = \eta A v/d\).
  3. \(F = 0.85 \times 0.02 \times 0.04 / 0.002 = 0.34\) N.

Answer: 0.34 N

Worked example · Derivation (Q1 pattern)

A cube of side \(a\) and density \(\rho\) slides down an incline of angle \(\theta\) on a thin oil film of thickness \(t\), at constant speed \(v\). Find η. Then evaluate for a 10 cm wooden cube (ρ = 600 kg/m³), θ = 30°, t = 0.2 mm, v = 0.5 m/s.

Show solution
  1. Constant speed means zero net force along the incline: \(mg\sin\theta = \eta A \dfrac{v}{t}\).
  2. With \(m = \rho a^3\) and contact area \(A = a^2\): \(\rho a^3 g \sin\theta = \eta a^2 v/t\).
  3. \(\eta = \dfrac{\rho a g t \sin\theta}{v}\).
  4. Numbers: \(\eta = 600 \times 0.1 \times 9.8 \times 2\times10^{-4} \times 0.5 / 0.5 = 0.118\) Pa·s.

Answer: η = ρagt sinθ / v ≈ 0.12 Pa·s

Worked example · Velocity gradient (Q31 pattern)

A river is 8 m deep. Its surface water flows at 3 m/s and the water at the bed is at rest. Assuming the speed changes uniformly with depth, find the viscous stress between horizontal layers. (η of water = 10⁻³ Pa·s.)

Show solution
  1. Velocity gradient \(= 3/8 = 0.375\ \text{s}^{-1}\) (uniform, from 0 at the bed to 3 m/s at the top).
  2. Stress \(= F/A = \eta\, dv/dx = 10^{-3} \times 0.375\).

Answer: 3.75 × 10⁻⁴ N/m²

From your Test-06

★ Coaching extra

Viscous flow through a pipe: Poiseuille's law

A tap needs a pressure difference to keep water moving through a long pipe. Viscosity transfers momentum between neighbouring layers, and the layer touching a stationary wall has zero speed in the no-slip model. The flow is fastest at the axis. For fully developed, steady laminar flow of an incompressible Newtonian fluid through a straight circular tube, the speed profile is parabolic.

Let r be the inner tube radius, ℓ its length and ΔP the inlet-to-outlet pressure drop for a horizontal tube. Do not confuse tube radius r with distance s from the axis.

Volume flow rate
\[Q=\frac{\pi r^4\Delta P}{8\eta\ell}\]
Q in m³/s, r and ℓ in m, ΔP in Pa and η in Pa·s. Flow resistance is \(\Delta P/Q=8\eta\ell/(\pi r^4)\).
Symbols and assumptions: Q = volume flow rate (m³/s); r = inner pipe radius (m); ΔP = pressure drop (Pa); η = viscosity (Pa·s); ℓ = pipe length (m). The pipe is horizontal, circular, straight and has fully developed laminar flow with no slip.
Velocity profile
\[v(s)=\frac{\Delta P}{4\eta\ell}(r^2-s^2),\quad v_\text{max}=2\bar v\]
The area-averaged speed is \(\bar v=Q/(\pi r^2)\). Zero at the wall; maximum at s = 0.
Symbols and assumptions: v(s) = axial speed (m/s) at radial distance s from the axis (m); r = pipe radius (m); ΔP = pressure drop (Pa); η = viscosity (Pa·s); ℓ = pipe length (m); v_max = axis speed; v̄ = section-average speed. At s = r, v = 0.
Interactive

Radius matters to the fourth power

Predicted flow Q–
Mean speed–
Maximum speed–
Re (ρ = 1000 kg/m³)–

–

This is not ideal Bernoulli flow

In a constant-area horizontal pipe, speed may stay the same while pressure drops because viscosity dissipates mechanical energy. Ideal Bernoulli without a loss term cannot describe that pressure drop. Poiseuille's law does not apply to turbulent flow; a large predicted Reynolds number warns that the laminar prediction needs checking.

Worked example · Units and flow rate

Water (η = 1.0 × 10⁻³ Pa·s) passes through a 1 m long tube of inner radius 1 mm under a 100 Pa pressure difference. Find Q in the laminar model.

Show solution
  1. \(Q=\pi(10^{-3})^4(100)/(8\times10^{-3}\times1)=3.93\times10^{-8}\) m³/s.
  2. 1 m³ = 10⁶ mL, so Q = 0.0393 mL/s.
  3. \(\bar v=Q/(\pi r^2)=0.0125\) m/s and \(R_e=\rho\bar v(2r)/\eta=25\), consistent with laminar flow.

0.0393 mL/s; mean speed 0.0125 m/s

This extension connects viscosity to real pipe flow. Reference: OpenStax: viscosity and turbulence.

Check your understanding

9.5.1 CoreExam

Stokes' law and terminal velocity

A raindrop falling from a cloud 1 km up would reach about 140 m/s if there were no air, fast enough to hurt badly. Real raindrops arrive at only a few metres per second. Why? As a body falls through a fluid, the fluid drags on it, and the drag grows with speed. Soon the drag balances the pull of gravity, the net force becomes zero, and the body falls at a constant speed: its terminal velocity.

For a small sphere moving slowly through a viscous fluid (laminar flow around it), Stokes showed that the drag is:

Stokes' law
\[ F_v = 6\pi\eta r v \]
r = radius of sphere, v = its speed relative to the fluid. Drag ∝ η, ∝ r, ∝ v. Valid for small spheres at low speed (laminar flow).
Symbols and assumptions: F_v = drag magnitude (N); η = liquid viscosity (Pa·s); r = sphere radius (m); v = sphere speed relative to the liquid (m/s). Drag opposes that relative motion. The sphere is rigid and sufficiently far from walls; the Reynolds number must be very small.
Terminal velocity
\[ v_t = \frac{2 r^2 (\rho - \sigma) g}{9\eta} \]
ρ = density of the sphere, σ = density of the fluid. If σ > ρ, \(v_t\) is negative: the body rises (air bubble).
Symbols and assumptions: v_t = terminal settling speed (m/s); r = sphere radius (m); ρ = sphere density; σ = liquid density, both in kg/m³; g = gravitational acceleration (m/s²); η = viscosity (Pa·s). Here σ is a density, not stress or Poisson’s ratio. A negative result indicates upward motion; Stokes-flow assumptions must hold.

Where the formula comes from

Three forces act on a sphere of radius \(r\) falling through a fluid:

  • Weight, down: \(W = \tfrac43\pi r^3 \rho g\)
  • Buoyant force (upthrust), up: \(B = \tfrac43\pi r^3 \sigma g\)
  • Viscous drag, opposite to motion (up): \(F_v = 6\pi\eta r v\), which starts at zero and grows as \(v\) grows

At first \(F_v = 0\), so the sphere accelerates. As \(v\) rises, \(F_v\) rises, the net force shrinks and the acceleration falls. When \(F_v = W - B\), the net force is zero and \(v\) stays fixed:

\[ 6\pi\eta r v_t = \tfrac43\pi r^3(\rho - \sigma)g \;\Rightarrow\; v_t = \frac{2r^2(\rho-\sigma)g}{9\eta} \]

Interactive

Ball falling through a viscous liquid

Terminal velocity–
Time constant–
Drag at vₜ (= W − B)–

Drop, then double r and drop again: the plateau rises 4×, not 2×. Make ρ smaller than σ to see the ball rise like an air bubble. The faint curves are your previous runs.

The v–t graph

Speed rises quickly at first, then levels off and approaches \(v_t\) without crossing it: \(v = v_t\,(1 - e^{-t/\tau})\) with \(\tau = 2\rho r^2/9\eta\). Acceleration starts at \(g(1-\sigma/\rho)\), not \(g\), because buoyancy acts from the start, and falls to zero. The distance–time graph curves at first and then becomes a straight line (constant speed). For small drops τ is only milliseconds, so they reach terminal velocity almost at once.

Exam trap · your Q24, Q30, Q13
  • \(v_t \propto r^2\), not \(r\) (Q24). The assertion “a bigger raindrop falls faster” is true; the reason “\(v_t \propto r\)” is false.
  • \(v_t \propto r^2\) only when the density is fixed. If the mass is fixed (and buoyancy is ignored), \(mg = 6\pi\eta r v_t\) gives \(v_t \propto 1/r\). Same mass, double radius: speed halves (Q30).
  • At a given speed, drag \(\propto r\). Since cross-section area \(A = \pi r^2\), drag \(\propto \sqrt{A}\), i.e. \(A^{1/2}\) (Q13).
At terminal velocity (Q45)
\[ F_v = W - B = \tfrac43\pi r^3(\rho-\sigma)g = Mg\left(1-\tfrac{\sigma}{\rho}\right) \]
If σ = ρ/2, the viscous force is Mg/2.
Symbols and assumptions: F_v = upward viscous drag (N); W = weight (N); B = buoyant force (N), not bulk modulus; M = sphere mass (kg); r = sphere radius (m); ρ = sphere density; σ = liquid density (kg/m³); g = gravitational acceleration (m/s²). This form describes a sphere settling downward.
n drops coalesce (Q32)
\[ R = n^{1/3}r,\quad v' = n^{2/3}\,v \]
Volume adds, so \(R^3 = nr^3\). Breaking one sphere into n equal drops: each has \(v/n^{2/3}\) (Q40: 27 pieces → speed ÷ 9).
Symbols and assumptions: n = number of identical initial drops; r = each small radius; R = merged radius, in matching units; v = initial terminal speed; v′ = merged terminal speed (m/s). Densities and viscosity stay unchanged; both speeds must be in the Stokes regime.
Rising air bubble (Q41)
\[ v = \frac{2r^2\sigma g}{9\eta} \;\Rightarrow\; \eta = \frac{2r^2\sigma g}{9v} \]
Air density ≈ 0 compared with the liquid density σ, so \(\rho - \sigma \approx -\sigma\): the bubble moves up.
Symbols and assumptions: v = steady upward speed (m/s); r = bubble radius (m); σ = solution density (kg/m³); g = gravitational acceleration (m/s²); η = solution viscosity (Pa·s). Air weight is neglected and the school model assumes Stokes-type drag; a clean mobile bubble interface can behave differently.
Falling-ball method to measure η

Drop a small steel ball into a tall jar of the liquid. Once it reaches its terminal velocity, time it between two marks to get \(v_t\), then use \(\eta = 2r^2(\rho-\sigma)g/9v_t\). Start timing well below the surface, after the ball has stopped speeding up.

Worked example · Ratio (Q3 pattern)

A copper ball (8.9 g/cc) and an aluminium ball (2.7 g/cc) of the same radius fall through glycerine (1.3 g/cc). The copper ball's terminal speed is 0.38 m/s. Find the aluminium ball's.

Show solution
  1. Same r and η, so \(v_t \propto (\rho-\sigma)\). Do not use the density ratio itself.
  2. \(\dfrac{v_{Al}}{v_{Cu}} = \dfrac{2.7-1.3}{8.9-1.3} = \dfrac{1.4}{7.6}\).
  3. \(v_{Al} = 0.38 \times 1.4/7.6 = 0.07\) m/s.

Answer: 0.07 m/s

Worked example · Numerical (Q44 pattern)

A steel ball of radius 2 mm (density 7800 kg/m³) reaches a terminal speed of 3 cm/s in an oil of density 900 kg/m³. Find the viscosity of the oil. (g = 9.8 m/s²)

Show solution
  1. \(\eta = \dfrac{2r^2(\rho-\sigma)g}{9v_t} = \dfrac{2 \times (2\times10^{-3})^2 \times 6900 \times 9.8}{9 \times 0.03}\).
  2. Numerator \(= 2 \times 4\times10^{-6} \times 6900 \times 9.8 = 0.541\); denominator \(= 0.27\).

Answer: η ≈ 2.0 Pa·s

Worked example · Coalescing & ratios (Q32, Q37 pattern)

(a) 27 identical rain droplets, each falling at terminal speed \(v\), merge into one drop. New terminal speed? (b) A ball of radius R and density 2σ falls in a liquid of density σ with terminal speed V. A ball of radius R/2 and density 5σ falls in the same liquid. Its terminal speed?

Show solution
  1. (a) \(R = 27^{1/3} r = 3r\). \(v_t \propto r^2\), so \(v' = 9v\).
  2. (b) \(v_t \propto r^2(\rho-\sigma)\). Old: \(R^2(2\sigma - \sigma) = R^2\sigma\). New: \((R/2)^2(5\sigma-\sigma) = R^2\sigma\). Same!

Answer: (a) 9v (b) V

Worked example · Concept (Q30 pattern)

Two spheres have the same mass, but one has three times the radius of the other. Ignoring buoyancy, compare their terminal speeds in the same liquid.

Show solution
  1. At terminal speed, \(mg = 6\pi\eta r v_t \Rightarrow v_t = mg/6\pi\eta r\).
  2. Same m, so \(v_t \propto 1/r\). The bigger sphere is less dense, which is why the \(r^2\) rule does not apply.

Answer: the larger sphere falls at one-third the speed

From your Test-06

★ Coaching extra Core

Reynolds number: smooth or chaotic?

Open a tap a little: the stream is smooth and glassy. Open it fully: the water churns and turns white. Smoke from an incense stick rises in a smooth thread, then suddenly breaks into curls. Slow flow is laminar; fast flow becomes turbulent, full of eddies.

Which one you get depends on a contest between two effects. Inertia (ρ and v) keeps a moving lump of fluid going and lets disturbances grow. Viscosity (η) damps disturbances and keeps layers orderly. The Reynolds number measures the ratio of the two:

Reynolds number
\[ R_e = \frac{\rho v d}{\eta} = \text{inertia/viscosity scale} \]
ρ = fluid density, v = flow speed, d = pipe diameter, η = viscosity. Dimensionless (no unit). Approximate ranges used in your coaching test: \(R_e \lt 1000\) laminar · 1000–2000 unsteady · \(R_e \gt 2000\) turbulent.
Symbols and assumptions: R_e = Reynolds number, dimensionless; ρ = fluid density (kg/m³); v = mean pipe speed (m/s); d = pipe diameter (m); η = viscosity (Pa·s). The force ratio represents a characteristic scaling, not a universal equality for every geometry.
Interactive

Reynolds' dye experiment

Regime–
Water speed, 1 cm pipe–

A thin thread of dye is injected on the axis. At low Re it stays a straight line; above about 2000 it wobbles, breaks into eddies and mixes across the whole pipe.

How it is asked · your Q20

“If the Reynolds number is greater than 2000, the flow is ___ and ___ forces dominate.” Answer: turbulent; inertial. A large \(R_e\) means inertia beats viscosity. Turbulence is more likely for fast flow, wide pipes, dense and less viscous fluids. Critical speed: \(v_c = R_e\,\eta/\rho d\).

Note

Use the 1000/2000 convention for the questions in your coaching paper. These are approximate teaching ranges, not universal transition thresholds. The actual onset of turbulence depends on geometry and disturbances; follow the convention stated in a question.

Worked example · Numerical

(a) Water (ρ = 1000 kg/m³, η = 10⁻³ Pa·s) flows at 15 cm/s through a pipe of diameter 2 cm. What type of flow is it? (b) What is the largest speed for steady laminar flow (\(R_e\) = 1000) in a 1 cm pipe?

Show solution
  1. (a) \(R_e = \rho v d/\eta = 1000 \times 0.15 \times 0.02/10^{-3} = 3000 \gt 2000\), so the flow is turbulent.
  2. (b) \(v = R_e\eta/\rho d = 1000 \times 10^{-3}/(1000 \times 0.01) = 0.1\) m/s.

Answer: (a) turbulent (Re = 3000) (b) 10 cm/s

From your Test-06

9.6–9.6.1 BasicsCore

Surface tension: a liquid's stretched skin

Lay a needle gently on water and it floats, even though steel is 8 times denser than water. Insects like water striders walk on ponds, and you can see the surface dimpling under their feet. Small drops are round. Wet paint-brush hairs spread out under water but clump together when you pull the brush out. All of these show that a liquid surface behaves like a stretched elastic skin.

9.6.1 · Surface energy: the molecular picture

Molecules in a liquid attract each other, but only over a short range (a few molecular diameters). A molecule deep inside is pulled equally in all directions, so the net force on it is zero. A molecule at the surface has neighbours below and beside it but almost none above, so it feels a net inward (downward) pull.

Bringing a molecule from inside up to the surface means working against this pull, and the molecule also loses some of its bonds. So surface molecules have extra energy compared with inside ones. A liquid therefore tends to keep its surface area as small as possible. For a given volume, a sphere has the least area, which is why drops are round.

Interactive

Why surface molecules are pulled inward

Neighbours in range–
Net force–

Tap a highlighted molecule to select it, then tap anywhere in the liquid to move it (or drag with a mouse). The dashed circle is its range of attraction.

Definition

Surface tension \(T\) (or S) is the force per unit length acting on an imaginary line drawn on the liquid surface. The force is perpendicular to the line and tangent to the surface: \(T = F/L\). Equivalently, it is the surface energy per unit area (next section).

Surface tension
\[ T = \frac{F}{L} \]
Unit N m⁻¹ (= J m⁻²). Dimensions [M T⁻²]. Water at 20 °C: ≈ 0.072 N/m. Soap solution: ≈ 0.03 N/m. Mercury: ≈ 0.47 N/m.
Symbols and assumptions: T = surface tension (N/m); F = tangential force (N) across a line of length L (m) on one liquid surface. The line lies in the surface; the force is perpendicular to that line. T here is not temperature.
Film on a frame (two surfaces)
\[ F = 2TL \]
A soap film has a front and a back surface, so a slider of length L is pulled by both: \(T L + T L\).
Symbols and assumptions: F = force pulling the movable wire (N); T = surface tension (N/m); L = wire length in contact with one face of the film (m). Both faces contribute, giving the factor 2.
Interactive

Soap film on a U-frame

Force F = 2TL–
Work F·Δx–
New area (2 faces)–

The pull does not depend on how far out the slider is. Unlike a spring, the film just adds new surface; its tension stays T.

Exam trap · your Q27, Q26
  • Surface tension is a scalar (Q27). The force due to it has a direction (along the surface, perpendicular to the line), but T itself has no fixed direction. “Surface tension is a vector” is the wrong statement.
  • Temperature: T decreases as temperature rises (cohesion weakens) and becomes zero at the critical temperature.
  • Impurities: a highly soluble impurity such as NaCl raises T. Sparingly soluble ones such as soap or detergent lower T. Oil, grease or dust on the surface also lower it (Q26).

Minimum force to pull something off a liquid surface

When you lift an object off a liquid surface, the liquid clings to its edges and pulls down with \(T\) on every metre of edge the liquid touches. Count every contact line; a wire touched on both sides counts twice.

Needle / wire, length l 2 contact lines F = 2lT (+ weight) Disc / plate, radius R outer edge only F = 2πRT Disc with hole (R, r) outer + inner edge F = 2π(R + r)T Square wire frame, side l each wire: inside + outside F = 2 × 4l × T = 8lT
Side views of objects being lifted. Red arrows show where surface tension pulls down. A thin ring of radius R (wire) is touched inside and outside: F = 2 × 2πR × T = 4πRT.
Exam trap · your Q25, Q5

A solid disc has only its outer rim in contact: \(2\pi RT\). A disc with a hole has two rims: \(2\pi(R+r)T\). A wire frame is wetted on both sides of every wire: a square of side \(l\) gives \(8lT\), not \(4lT\). A needle of length \(l\) has a contact line on each side: \(2lT\).

Worked example · Numerical (Q28 pattern)

A U-frame holds a water film. Its sliding wire is 5 cm long. The film just supports the slider plus a hanging weight, total 7.2 × 10⁻³ N. Find T.

Show solution
  1. The film has two surfaces: upward force \(= 2TL\).
  2. \(2T(0.05) = 7.2\times10^{-3} \Rightarrow T = 7.2\times10^{-3}/0.1\).

Answer: T = 0.072 N/m (if you forget the factor 2 you get 0.144, which is a common wrong option)

Worked example · Floating needle (Q29 pattern)

Show that the largest diameter of a steel needle that can float on water is \(d = \sqrt{8T/\pi\rho g}\), and evaluate it for ρ = 7800 kg/m³, T = 0.072 N/m. (Ignore buoyancy.)

Show solution
  1. Per unit length, weight \(= \dfrac{\pi d^2}{4}\rho g\).
  2. The maximum upward pull comes when the surface on both sides becomes vertical: \(2T\) per unit length.
  3. \(\dfrac{\pi d^2 \rho g}{4} = 2T \Rightarrow d = \sqrt{\dfrac{8T}{\pi\rho g}} = \sqrt{\dfrac{8 \times 0.072}{\pi \times 7800 \times 9.8}}\).

Answer: d ≈ 1.5 × 10⁻³ m = 1.5 mm

Worked example · Concept (Q4 pattern)

A thin disc of radius r floats on water. At its rim the water surface meets the disc making an angle θ with the vertical. The disc displaces water of weight W. What is the weight of the disc?

Show solution
  1. Upward forces: buoyancy W, plus surface tension along the rim. The rim length is \(2\pi r\), and the pull is along the surface, at θ to the vertical, so its vertical part is \(T\cos\theta\) per unit length.
  2. Equilibrium: weight \(= W + 2\pi r T\cos\theta\).

Answer: W + 2πrT cos θ

From your Test-06

9.6.1–9.6.2 CoreExam

Surface energy: making new surface costs work

Every surface molecule carries extra energy. To make more surface you must haul molecules up from inside, so you must do work. That work is stored as surface energy. Go back to the U-frame: pull the slider out by \(\Delta x\) against the force \(2TL\). The work is \(2TL\Delta x\), and the new area created is \(L\Delta x\) on each of the two faces, \(2L\Delta x\) in total. So

\[ W = T \times (\text{total new area}) \quad\Rightarrow\quad T = \frac{W}{\Delta A} \]

Surface tension is therefore also the surface energy per unit area. N/m and J/m² are the same unit.

Film (two surfaces)
\[ W = T \cdot 2\,\Delta A \]
ΔA = change in area of the film as you see it (one face).
Symbols and assumptions: W = work to increase surface area (J); T = constant surface tension (N/m); ΔA = increase in area of one face (m²). The total new area is 2ΔA.
Soap bubble, r₁ → r₂
\[ W = 8\pi T\,(r_2^2 - r_1^2) \]
Two surfaces, each \(4\pi r^2\). Blowing from zero: \(8\pi r^2T\).
Symbols and assumptions: W = increase in surface energy (J); T = surface tension (N/m); r₁, r₂ = initial/final bubble radii (m). This counts two surfaces of a thin soap film and assumes T stays constant.
Liquid drop (one surface)
\[ E = 4\pi r^2 T \]
A drop has only its outer surface.
Symbols and assumptions: E = surface energy (J); r = drop radius (m); T = surface tension (N/m). The drop has area 4πr² and one liquid–air interface; creating extra area increases E.
n small drops → one big drop
\[ \Delta E = 4\pi r^2 T\, n\,(1 - n^{-1/3}) = 4\pi R^2 T\,(n^{1/3}-1) \]
Volume conserved, \(R = n^{1/3} r\). Energy is released (as heat). Splitting R into n drops needs this much work.
Symbols and assumptions: ΔE = positive energy released (J); n = number of equal small drops; r = each small radius (m); R = merged radius (m); T = surface tension (N/m). Volume conservation gives R³ = nr³; surface area decreases.
Exam trap · your Q7, Q15
  • When drops merge, total volume stays the same but total surface area decreases, so surface energy is liberated (the big drop warms slightly). Nothing about “mass is converted into energy”: mass is conserved here (Q7).
  • Two equal drops of radius r merge: \(R = 2^{1/3}r\), energy released \(= T[2(4\pi r^2) - 4\pi R^2] = 4\pi r^2 T\,(2 - 2^{2/3})\) (Q15).
  • Splitting one drop into many needs energy, since you are creating surface.
Temperature rise when drops merge

Energy released heats the big drop: \(\Delta\theta = \dfrac{3T}{\rho s}\left(\dfrac1r - \dfrac1R\right)\), where s is the specific heat (J kg⁻¹ K⁻¹).

Worked example · Film (Q21 pattern)

A rectangular soap film is stretched from 8 cm × 5 cm to 8 cm × 10 cm. The work done is 5.76 × 10⁻⁴ J. Find T.

Show solution
  1. Change in area of one face: \(8\times10 - 8\times5 = 40\ \text{cm}^2 = 4\times10^{-3}\ \text{m}^2\).
  2. Two faces: total new area \(= 8\times10^{-3}\ \text{m}^2\).
  3. \(T = W/\Delta A_{total} = 5.76\times10^{-4}/8\times10^{-3}\).

Answer: T = 0.072 N/m

Worked example · Bubble (Q33 pattern)

A soap bubble (T = 3 × 10⁻² N/m) is blown from radius 1 cm to radius 3 cm. Work done?

Show solution
  1. \(W = 2 \times 4\pi(r_2^2 - r_1^2) \times T = 8\pi T(r_2^2 - r_1^2)\).
  2. \(= 8\pi \times 0.03 \times (9 - 1)\times10^{-4} = 8\pi \times 0.03 \times 8\times10^{-4}\).

Answer: W ≈ 6.0 × 10⁻⁴ J (watch out: diameters in the question → halve them first)

Worked example · Splitting

A water drop of radius 1 mm (T = 0.072 N/m) is sprayed into 1000 identical droplets. How much work is needed?

Show solution
  1. \(r = R/1000^{1/3} = R/10\). New area \(= 1000 \times 4\pi (R/10)^2 = 10 \times 4\pi R^2\).
  2. Increase in area \(= 9 \times 4\pi R^2\), i.e. \(4\pi R^2(n^{1/3}-1)\).
  3. \(W = 9 \times 4\pi \times 10^{-6} \times 0.072 \approx 8.1\times10^{-6}\) J.

Answer: ≈ 8.1 × 10⁻⁶ J

From your Test-06

9.6.3 BasicsCore

Angle of contact: does the liquid wet the solid?

Water dropped on clean glass spreads into a thin patch. Water on a lotus leaf or a waxy, greasy surface rolls into beads. Mercury on glass forms shiny balls. The difference is a tug-of-war between two attractions:

  • Cohesion: liquid molecules attracting each other.
  • Adhesion: liquid molecules attracting the solid.

If adhesion wins, the liquid spreads over the solid (it wets it). If cohesion wins, the liquid pulls itself into a ball.

Definition

The angle of contact θ is the angle between the tangent to the liquid surface at the point of contact and the solid surface, measured inside the liquid. It depends on the pair of materials (and on cleanliness), not on the amount of liquid.

Balance of surface tensions at the contact line (NCERT)
\[ S_{la}\cos\theta + S_{sl} = S_{sa} \;\Rightarrow\; \cos\theta = \frac{S_{sa}-S_{sl}}{S_{la}} \]
l = liquid, s = solid, a = air. If \(S_{sl} \gt S_{sa}\), cos θ < 0, so θ is obtuse (does not wet, e.g. water–leaf). If \(S_{sl} \lt S_{sa}\), θ is acute (wets, e.g. water–glass).
Symbols and assumptions: S_la = liquid–air surface tension; S_sl = solid–liquid interfacial energy per area; S_sa = solid–air interfacial energy per area, all in N/m = J/m². θ = equilibrium contact angle measured through the liquid. This balance assumes a smooth equilibrium contact line.
Interactive

Contact angle: drop shape and meniscus

Wets?–
Meniscus–
In capillary–
θ < 90° (acute)θ = 90°θ > 90° (obtuse)
AttractionAdhesion > cohesionBalancedCohesion > adhesion
WettingWets the solid–Does not wet
Meniscus in tubeConcave (curves down in the middle)FlatConvex (bulges up)
CapillaryRisesNo rise or fallFalls (depression)
ExampleWater–clean glass (≈ 0°)Water–silver (often quoted)Mercury–glass (≈ 140°)
How it is asked · your Q6, Q8

“The angle of contact for a non-wetting liquid is ___” → obtuse. “A convex meniscus means θ is ___” → greater than 90°. Concave ↔ acute ↔ rises. Convex ↔ obtuse ↔ falls.

Detergents and waterproofing

Soaps and detergents lower surface tension and reduce θ, so water wets cloth and soaks into the tiny gaps where dirt sits; dirt and grease are then held in the water and washed away. Waterproofing agents do the opposite: they make θ large (obtuse), so water beads up and rolls off instead of soaking in.

Worked example · Statement I / II

Statement I: Adding detergent to water increases the angle of contact between water and cloth. Statement II: Detergents reduce the surface tension of water.

Show solution
  1. Detergent helps water wet the cloth, so θ decreases. Statement I is false.
  2. Detergent lowers T. Statement II is true.

Answer: Statement I false, Statement II true

From your Test-06

9.6.4 CoreExam

Drops and bubbles: excess pressure inside

A curved liquid surface acts like a stretched balloon skin and squeezes what is inside. So the pressure on the concave side (inside) of a curved surface is higher than on the convex side (outside). The more curved the surface, i.e. the smaller the radius, the bigger the squeeze. That is why a balloon is hardest to blow at the very start.

Derivation for a drop (energy method)

Let a drop of radius \(r\) have excess pressure \(P_{ex} = P_{in} - P_{out}\). Imagine it grows to \(r + \Delta r\):

  • Work done by the excess pressure \(= P_{ex} \times \Delta V = P_{ex}\,4\pi r^2\Delta r\)
  • Increase in surface energy \(= T\,\Delta A = T\,8\pi r\Delta r\)

Equating them gives \(P_{ex} = 2T/r\). A soap bubble has two surfaces, so its \(\Delta A\) doubles, giving \(4T/r\). An air bubble inside a liquid has only one surface (liquid–air), giving \(2T/r\). The simulation shows the same result by force balance on half the drop.

Liquid drop
\[ P_{in}-P_{out} = \frac{2T}{r} \]
One surface (outer).
Symbols and assumptions: P_in, P_out = pressures inside/outside the drop (Pa); T = surface tension (N/m); r = spherical drop radius (m). Their difference is the excess pressure, not the full inside pressure.
Soap bubble in air
\[ P_{in}-P_{out} = \frac{4T}{r} \]
Two surfaces (outer and inner).
Symbols and assumptions: P_in, P_out = inside/outside pressures (Pa); T = surface tension (N/m); r = bubble radius (m). A thin film has two surfaces, giving twice the drop’s excess pressure.
Air bubble at depth h in a liquid
\[ P_{in} = P_0 + \rho g h + \frac{2T}{r} \]
One surface. P₀ = atmospheric pressure on the liquid.
Symbols and assumptions: P_in = bubble inside pressure (Pa); P₀ = pressure on the liquid free surface (Pa); ρ = surrounding liquid density (kg/m³); g = gravitational acceleration (m/s²); h = bubble depth (m); T = liquid–air surface tension (N/m); r = bubble radius (m).
Interactive

One surface or two? Excess pressure by force balance

Surfaces–
Excess pressure–
Surface energy–

Cut the object in half. The excess pressure pushes the right half to the right over area πr². Surface tension holds it back along the rim, 2πr long, once per surface.

Liquid dropSoap bubble (in air)Air bubble (in liquid)
Free surfaces121
Excess pressure2T/r4T/r2T/r
Surface energy4πr²T8πr²T4πr²T
Work to grow r₁ → r₂4πT(r₂² − r₁²)8πT(r₂² − r₁²)4πT(r₂² − r₁²)
Total pressure insideP₀ + 2T/rP₀ + 4T/rP₀ + ρgh + 2T/r

Two bubbles connected: the small one empties into the big one

Since \(P_{ex} = 4T/r\), the smaller bubble has the higher pressure. Connect two bubbles and air flows from small to large. The small bubble shrinks, its pressure rises further, and it keeps emptying. It stops only when it has become a shallow cap on its tube whose radius of curvature equals that of the big bubble.

Interactive

Open the valve between two soap bubbles

Excess P, bubble 1–
Excess P, bubble 2–
Air flows–

T = 0.03 N/m. Notice the moment bubble 1 becomes a hemisphere: that is its smallest radius of curvature, so its pressure peaks there. After that it flattens into a cap.

Exam trap · your Q17, Q19
  • Q17 (A–R): “the bigger bubble grows and the smaller shrinks” is true, and “pressure inside is inversely proportional to radius” is the correct explanation.
  • Q19: on equal tube mouths, a hemispherical bubble has the smallest possible radius of curvature (= the mouth radius), so it has the highest pressure. A less-than-hemisphere cap is flatter (bigger radius of curvature, lower pressure). Air flows from the hemisphere (1) to the other (2), and bubble 1 shrinks.
Common interface of two stuck bubbles
\[ r = \frac{r_1 r_2}{r_2 - r_1} \]
From \(\frac{4T}{r_1} - \frac{4T}{r_2} = \frac{4T}{r}\) (r₁ < r₂). The interface bulges into the bigger bubble.
Symbols and assumptions: r = radius of curvature of the common film (m); r₁, r₂ = radii of the two bubbles (m), with r₁ < r₂; T = soap-film surface tension (N/m). For equal bubble radii, the separating film is flat, corresponding to infinite r.
Moles of air in a bubble
\[ n = \frac{PV}{RT_K} = \frac{\left(P_0 + \frac{4T}{r}\right)\frac43\pi r^3}{RT_K} \]
Use the inside pressure (Q18). \(T_K\) = absolute temperature. If two bubbles merge isothermally in vacuum (P₀ = 0): \(R^2 = r_1^2 + r_2^2\).
Symbols and assumptions: n = amount of gas (mol); P = absolute inside pressure (Pa); V = gas volume (m³); R in PV/(RT_K) = universal gas constant 8.314 J/(mol·K); T_K = gas temperature (K); T = surface tension (N/m); r = bubble radius (m); P₀ = outside pressure (Pa). In the merger result, R instead denotes the final bubble radius: read each R in its local context.
Worked example · Numerical (Q35 pattern)

An air bubble of radius 0.2 mm is 10 cm below the surface of water. The pressure inside it exceeds atmospheric pressure by 1700 Pa. Find T. (ρ = 1000 kg/m³, g = 10 m/s²)

Show solution
  1. \(P_{in} - P_0 = \rho g h + 2T/r\).
  2. \(\rho g h = 1000 \times 10 \times 0.1 = 1000\) Pa, so \(2T/r = 700\) Pa.
  3. \(T = 700 \times 2\times10^{-4}/2 = 0.07\) N/m.

Answer: T = 0.07 N/m

Worked example · Ratio of moles (Q18 pattern)

Soap bubbles A (radius 1 cm) and B (radius 2 cm) are inside a chamber kept at 4 N/m². T = 0.02 N/m, same temperature. Find \(n_B/n_A\).

Show solution
  1. \(P_A = 4 + \dfrac{4(0.02)}{0.01} = 12\) N/m². \(P_B = 4 + \dfrac{4(0.02)}{0.02} = 8\) N/m².
  2. \(n \propto PV \propto Pr^3\): \(\dfrac{n_B}{n_A} = \dfrac{8 \times 2^3}{12 \times 1^3} = \dfrac{64}{12}\).

Answer: 16/3 ≈ 5.3

Worked example · Interface

Two soap bubbles of radii 4 cm and 6 cm stick together. Radius of curvature of the common film?

Show solution
  1. \(r = r_1r_2/(r_2 - r_1) = 24/2\).

Answer: 12 cm, bulging into the 6 cm bubble

Worked example · Exam level (Q20b pattern)

A liquid drop of density ρ floats half-immersed in another liquid of density σ. The surface tension of the drop's liquid is T. Find the radius of the drop.

Show solution
  1. Weight (down): \(\tfrac43\pi r^3\rho g\).
  2. Buoyancy on the immersed hemisphere (up): \(\tfrac23\pi r^3\sigma g\).
  3. Surface tension acts along the waterline circle at the equator (length \(2\pi r\)) and pulls vertically up: \(2\pi r T\).
  4. \(\tfrac43\pi r^3\rho g = \tfrac23\pi r^3\sigma g + 2\pi rT \Rightarrow r^2 g\,\dfrac{2(2\rho-\sigma)}{3} = 2T\).

Answer: \(r = \sqrt{\dfrac{3T}{g(2\rho - \sigma)}}\)

From your Test-06

9.6.5 CoreExam

Capillary rise: water climbing a thin tube

Dip the corner of a paper towel in water and the water climbs up the towel. A lamp wick lifts oil to the flame. Blotting paper drinks ink. A sugar cube sucks up tea. Water rises through the tiny gaps in soil to plant roots. Each of these is a network of very thin tubes, and liquid rises in thin tubes. This is capillarity (capilla = hair, as in hair-thin).

Why it rises: excess pressure again

Water wets glass, so inside a thin glass tube its surface (meniscus) is concave, curving down in the middle. Just below a concave surface the pressure is lower than just above it (above is the inside of the curve, below is the outside). So:

  1. Just above the meniscus the pressure is atmospheric, \(P_0\).
  2. Just below the meniscus it is \(P_0 - 2T/R\), where R is the radius of the meniscus.
  3. Outside the tube, at the flat water surface, the pressure is \(P_0\). Liquid is pushed up the tube until the column's weight makes up the difference: \(h\rho g = 2T/R\).
  4. Geometry: the meniscus meets the wall at θ, so \(R = r/\cos\theta\) (r = inner radius of the tube). For water–glass, θ ≈ 0 and R = r (a hemisphere).
Capillary rise (Jurin's law)
\[ h = \frac{2T\cos\theta}{r\rho g} \]
r = inner radius. θ > 90° gives h < 0 (fall, e.g. mercury). \(h \propto 1/r\), so \(hr\) = constant for a given liquid.
Symbols and assumptions: h = signed vertical rise above the outside liquid level (m); T = surface tension (N/m); θ = contact angle through the liquid; r = tube inner radius (m); ρ = liquid density (kg/m³); g = gravitational acceleration (m/s²). Negative h means capillary depression.
Force method: weight held up
\[ \pi r^2 h\rho g = 2\pi r T\cos\theta \]
Surface tension pulls up all round the rim. The weight of the column is \(2\pi rT\cos\theta\): independent of h, and ∝ r. So the mass raised ∝ r.
Symbols and assumptions: r = inner tube radius (m); h = vertical rise (m); ρ = liquid density (kg/m³); g = gravitational acceleration (m/s²); T = surface tension (N/m); θ = contact angle through the liquid. The left side is the raised column’s weight; the right is the upward component of force around its rim.
Measuring T by capillary rise
\[ T = \frac{r h \rho g}{2\cos\theta} \;\xrightarrow{\theta\,\approx\,0}\; \frac{rh\rho g}{2} \]
Measure h with a travelling microscope and the bore radius r. A finer version adds the meniscus volume: \(T = r(h + r/3)\rho g/2\).
Symbols and assumptions: T = inferred surface tension (N/m); r = measured inner radius (m); h = vertical rise to the meniscus bottom (m); ρ = liquid density (kg/m³); g = gravitational acceleration (m/s²); θ = contact angle. The h + r/3 correction assumes a nearly hemispherical meniscus at θ ≈ 0.
Interactive

Capillary tube lab

Height h–
Meniscus radius–
Column weight–

–

Exam traps · your Q9, Q10, Q14, Q16, Q34
  • Depends on the inner radius of the tube, not its mass, wall thickness or outer radius (Q16; you chose mass of tube).
  • Tilted tube: the vertical height stays h. The length of liquid along the tube is \(l = h/\cos\alpha\), with α measured from the vertical. At 60°, \(l = 2h\) (Q9: 2 cm → 4 cm). If the angle is given from the horizontal, use \(l = h/\sin\).
  • Tube shorter than h: the liquid rises to the top but does not overflow. The meniscus becomes flatter (its radius grows) so that \(hR\) = constant: \(R' = Rh/l\) (Q14). No perpetual-motion fountain.
  • Free fall / satellite: effective g = 0, so the liquid rises and fills the whole tube, whatever its length (Q10: fills all 30 cm). On the Moon (g/6) the rise is 6h if the tube is long enough. In a lift accelerating up, \(g_{eff} = g + a\) and h decreases.
  • Mass raised ∝ r: double the radius, double the mass, even though h halves (Q34: 2M).
Worked example · Numerical (Q11 pattern)

Water (θ = 0) rising in a capillary of radius 0.5 mm holds up a column weighing 2.26 × 10⁻⁴ N. Find T.

Show solution
  1. Weight held = upward surface-tension force \(= 2\pi r T\cos\theta = 2\pi r T\).
  2. \(T = 2.26\times10^{-4}/(2\pi \times 5\times10^{-4}) = 2.26\times10^{-4}/3.14\times10^{-3}\).

Answer: T ≈ 0.072 N/m

Worked example · Tilted tube (Q9 pattern)

Water rises 3 cm in a vertical capillary. The tube is tilted to 53° from the vertical (cos 53° ≈ 0.6). (a) Vertical height of the water column? (b) Length of tube wetted?

Show solution
  1. (a) The pressure balance involves only the vertical height, so it is still 3 cm.
  2. (b) \(l = h/\cos\alpha = 3/0.6 = 5\) cm.

Answer: (a) 3 cm (b) 5 cm

Worked example · Measuring T

In the capillary rise method, water rises 6.0 cm in a clean glass tube of bore radius 0.24 mm. Find T (θ = 0, g = 9.8 m/s²).

Show solution
  1. \(T = rh\rho g/2 = 0.24\times10^{-3} \times 0.06 \times 1000 \times 9.8/2\).

Answer: T ≈ 0.071 N/m

Worked example · Concept (Q14 pattern)

Water would rise 8 cm in a capillary, but only 5 cm of the tube sticks out above the water. What happens?

Show solution
  1. The water reaches the top of the tube and stops; it cannot overflow, because once it reaches the top the meniscus simply changes shape.
  2. \(h \propto 1/R\) (meniscus radius), so \(R' = R \times 8/5 = 1.6R\). The meniscus flattens.

Answer: rises to the top (5 cm), no overflow; meniscus radius becomes 1.6 times

From your Test-06

9.6.5 Experiment

Determining surface tension by capillary rise

The syllabus specifically asks for this method. Knowing that a narrow tube makes water rise is the starting point; the experiment measures the rise and the inner radius to infer surface tension.

For a long, vertical, clean tube with a nearly circular bore, balance upward force \(2\pi rT\cos\theta\) against the weight \(\pi r^2h\rho g\) of the raised column. For clean water–glass, take \(\theta\approx0\) unless the question states otherwise.

School-level capillary-rise measurement
\[T=\frac{\rho grh}{2\cos\theta}\approx\frac{\rho grh}{2}\quad(\theta\approx0)\]
Measure h vertically from the outside free surface to the bottom of the concave meniscus. Use the bore radius, not the wall thickness or outer radius. This approximation neglects the small meniscus-volume correction.
Symbols and assumptions: T = inferred surface tension (N/m); ρ = liquid density (kg/m³); g = gravitational acceleration (m/s²); r = inner tube radius (m); h = vertical rise above the outside liquid surface (m); θ = contact angle measured through the liquid.

Apparatus and procedure

  1. Use a clean capillary held vertically in a beaker of clean water, a travelling microscope or suitable height scale, and a means of measuring the inner bore. Let the water settle and keep temperature approximately constant.
  2. Read the position of the bottom of the meniscus inside the capillary, keeping the line of sight level to avoid parallax.
  3. Read the outside water level using a pointer or the microscope. Subtract the two readings to obtain h; immersion depth below the outside level is not the capillary rise.
  4. Measure the inner diameter in two perpendicular directions at a suitable tube end. If the bore is nearly circular, average the readings and divide by two for r.
  5. Convert all lengths to metres and calculate T. Repeat height readings and report the measured temperature and assumptions.
Interactive

From two height readings to surface tension

Inferred T–
Maximum uncertainty–

This calculator infers T from measured r and h; its two sliders are independent measurements. It assumes θ = 0, ρ = 1000 kg/m³, g = 9.8 m/s² and neglects the meniscus correction. Tube width is exaggerated for visibility.

Errors, precautions and the small correction

For \(T=\rho grh/2\), if ρ and g are treated as exact, the first-order maximum fractional uncertainty is \(\Delta T/T\approx\Delta r/r+\Delta h/h\). Independent random uncertainties would normally combine differently; the sum is the school-level worst-case estimate.

Grease and impurities can change both surface tension and contact angle. A tilted tube gives a length along the tube rather than the vertical height. A tube shorter than its natural rise requires a changed meniscus, so it is unsuitable for the simple measurement.

For a nearly hemispherical meniscus at θ ≈ 0, the small extra liquid volume gives the refined expression \(T\approx\rho gr(h+r/3)/2\) when h is measured to the meniscus bottom. Use this correction only when requested; do not mix the corrected and uncorrected definitions of height.

Worked example · Measurement and uncertainty

Measured r = 0.24 mm and h = 6.0 cm for clean water–glass. Estimate T without the small correction. Radius and height uncertainties are 2% and 3%; treat ρ = 1000 kg/m³ and g = 9.8 m/s² as exact.

Show solution
  1. \(T=1000\times9.8\times0.24\times10^{-3}\times0.060/2=0.07056\) N/m.
  2. Maximum percentage uncertainty = 2 + 3 = 5%.
  3. Absolute uncertainty ≈ 0.05 × 0.07056 = 0.00353 N/m.

T ≈ (0.071 ± 0.004) N/m, with a 5% worst-case uncertainty

Check your understanding

★ Exam

Problem patterns & shortcuts

Almost every question in this half of the chapter is one of the patterns below. Spot the pattern, write the proportionality, and the numbers usually fall out in one line.

1 · Plate on a film / block on an incline

\(F = \eta A v/d\). On an incline at constant v: \(mg\sin\theta = \eta A v/t\). Convert poise → Pa·s (÷10) and cm² → m² (×10⁻⁴).

2 · Terminal velocity ratios

\(v_t \propto r^2(\rho-\sigma)/\eta\). Same ball in two liquids, or two balls in one liquid: use \((\rho-\sigma)\), never ρ alone.

3 · Merge / break drops (speed)

n drops → one: \(v \times n^{2/3}\) (8 → ×4, 27 → ×9, 64 → ×16). One → n: \(v/n^{2/3}\).

4 · Same mass, different size

No buoyancy: \(v_t = mg/6\pi\eta r \propto 1/r\). Double r → half v.

5 · Free fall, then enters liquid (Q22)

“Speed does not change on entering” means it enters at \(v_t\): \(\sqrt{2gh} = v_t \Rightarrow h = v_t^2/2g\). E.g. a 1 mm ball, ρ = 10.5 × 10³ in water: \(v_t \approx 20.7\) m/s, h ≈ 22 m.

6 · Viscous force at terminal speed (Q45)

\(F_v = W - B = Mg(1 - \sigma/\rho)\). Liquid half as dense as the ball: Mg/2.

7 · Film work: count two faces

\(W = 2T\Delta A\) for a film, \(8\pi T(r_2^2-r_1^2)\) for a bubble. Diameters given? Halve them first.

8 · Merging drops: energy

Released \(= 4\pi r^2 T\,n(1-n^{-1/3}) = 4\pi R^2T(n^{1/3}-1)\). Two drops: \(4\pi r^2T(2-2^{2/3})\). Temperature rise: \(\frac{3T}{\rho s}(\frac1r - \frac1R)\).

9 · Pull-off force

Needle 2lT · disc 2πRT · disc with hole 2π(R + r)T · thin ring 4πRT · square frame 8lT. Add the object's weight if asked for total force.

10 · Excess pressure

Drop and air bubble 2T/r, soap bubble 4T/r. At depth: \(P_0 + \rho gh + 2T/r\). Smaller bubble → higher pressure.

11 · Bubble combos

Interface \(r_1r_2/(r_2-r_1)\). Moles \(\propto (P_0 + 4T/r)r^3\). Merge in vacuum (isothermal): \(R^2 = r_1^2+r_2^2\).

12 · Capillary ratios

\(h \propto T\cos\theta/r\rho g\); \(hr\) = const; mass raised ∝ r; weight lifted \(= 2\pi rT\cos\theta\); tilted \(l = h/\cos\alpha\); g → 0 fills the tube; tube too short means no overflow.

QuantityFormulaSI unitDimensions
Coefficient of viscosity ηF d / (A v)Pa·s = N s m⁻²[M L⁻¹ T⁻¹]
Velocity gradientdv/dxs⁻¹[T⁻¹]
Reynolds numberρvd/ηnone[M⁰ L⁰ T⁰]
Surface tension TF/L = W/ΔAN m⁻¹ = J m⁻²[M T⁻²]
Surface energyT × AJ[M L² T⁻²]
Worked example · Dimensional analysis

Assume the drag on a sphere depends on η, r and v as \(F = k\,\eta^a r^b v^c\). Find a, b, c.

Show solution
  1. \([\mathrm{MLT^{-2}}] = [\mathrm{ML^{-1}T^{-1}}]^a[\mathrm{L}]^b[\mathrm{LT^{-1}}]^c\).
  2. M: a = 1. T: −a − c = −2 ⇒ c = 1. L: −a + b + c = 1 ⇒ b = 1.

Answer: F = k η r v (Stokes found k = 6π)

★ Revise

Night-before checklist

  • \(F = \eta A\,dv/dx\); η in Pa·s, 1 poise = 0.1 Pa·s; [ML⁻¹T⁻¹].
  • Liquids: η ↓ with T. Gases: η ↑ with T.
  • Ideal fluid η = 0. For Test-06, a lubricant needs enough viscosity to maintain its film; practical choice depends on operating conditions.
  • Poiseuille: \(Q=\pi r^4\Delta P/(8\eta\ell)\), fully developed laminar flow; axis speed = 2 × mean speed.
  • Stokes \(F = 6\pi\eta rv\); drag ∝ r ∝ √A, for creeping flow around a sphere.
  • \(v_t = 2r^2(\rho-\sigma)g/9\eta\): ∝ r², ∝ (ρ − σ). Same mass: ∝ 1/r.
  • n drops merge: v × n^{2/3}. At v_t: F_v = W − B.
  • Re = ρvd/η. Your coaching convention: < 1000 laminar, > 2000 turbulent with inertia dominant; thresholds depend on the flow setup.
  • T = F/L, N/m, [MT⁻²], scalar; T ↓ with temperature, 0 at critical temperature.
  • NaCl ↑ T; soap/detergent ↓ T.
  • Film: 2 surfaces → F = 2TL, W = 2TΔA. Frame side l: 8lT.
  • Merging drops release energy (not mass → energy).
  • Excess P: drop 2T/r, soap bubble 4T/r, air bubble 2T/r (+ρgh at depth). Small bubble empties into big one.
  • θ < 90°: wets, concave, rises. θ > 90°: convex, falls. Hg–glass ≈ 140°.
  • \(h = 2T\cos\theta/r\rho g\), inner r; hr const; mass ∝ r; tilted l = h/cos α; short tube: the meniscus changes shape. In ideal free fall, the gravity limit disappears; finite-tube behaviour depends on wetting and boundaries.
  • Capillary experiment: \(T=\rho grh/2\) for θ ≈ 0; use the inner radius and vertical rise. Maximum relative errors in r and h add.

More practice: all Test-06 questions · quick formulas: Revise · first half of the chapter: Fluids I.