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Fluid Mechanics & Surface Tension Formulas

Pascal's law, Archimedes principle, continuity equation, Bernoulli's theorem, viscosity (Stokes law, Poiseuille), and surface tension.

7 Formulas•368+ Questions in Bank

Core Formulas & Mathematical Identities

7
01

Continuity Equation & Bernoulli's Principle

A1v1=A2v2,P+12ρv2+ρgh=constantA_1 v_1 = A_2 v_2, \quad P + \frac{1}{2}\rho v^2 + \rho g h = \text{constant}

Mass and energy conservation in ideal streamline fluid flow.

Examiner Tip: Torricelli's speed of efflux: v = √(2gh).
02

Stokes' Law & Terminal Velocity

Fv=6πηrv,vt=29r2(ρ−σ)gηF_v = 6\pi\eta r v, \quad v_t = \frac{2}{9}\frac{r^2(\rho - \sigma)g}{\eta}

Viscous drag force on sphere and steady terminal fall speed.

Examiner Tip: Terminal velocity is proportional to the square of sphere radius (v_t ∝ r²).
03

Excess Pressure in Drops & Bubbles

ΔPdrop=2TR,ΔPsoap bubble=4TR\Delta P_{\text{drop}} = \frac{2T}{R}, \quad \Delta P_{\text{soap bubble}} = \frac{4T}{R}

Pressure difference across curved liquid interface due to surface tension T.

Examiner Tip: Soap bubble has 2 free surfaces, so excess pressure is doubled.
04

Capillary Rise (Jurin's Law)

h=2Tcos⁡θρgrh = \frac{2T\cos\theta}{\rho g r}

Height of liquid column climbing a capillary tube of radius r with contact angle θ.

Examiner Tip: For pure water in clean glass, contact angle θ ≈ 0° (cos θ = 1).
05

Torricelli's Law & Efflux Range

v=2gh,R=2h(H−h),Rmax=H  (at h=H/2),tempty=Aa2Hgv = \sqrt{2gh}, \quad R = 2\sqrt{h(H - h)}, \quad R_{\text{max}} = H \; (\text{at } h = H/2), \quad t_{\text{empty}} = \frac{A}{a}\sqrt{\frac{2H}{g}}

Speed of efflux from orifice at depth h below surface, horizontal range on ground, and total emptying time of tank.

Examiner Tip: Two holes at depths h and (H - h) yield identical horizontal ranges.
06

Poiseuille's Viscous Flow & Reynolds Number

Q=πΔPr48ηL,Re=ρvDηQ = \frac{\pi \Delta P r^4}{8\eta L}, \quad R_e = \frac{\rho v D}{\eta}

Volume flow rate Q through a circular capillary pipe and dimensionless Reynolds number determining flow stability.

Examiner Tip: Flow is laminar for R_e < 2000, unstable for 2000 < R_e < 3000, and turbulent for R_e > 3000.
07

Surface Energy & Droplet Coalescence

W=TΔA,R=n1/3r,ΔUreleased=4πTr2(n−n2/3),ΔT=3Tsρ(1r−1R)W = T \Delta A, \quad R = n^{1/3}r, \quad \Delta U_{\text{released}} = 4\pi T r^2 (n - n^{2/3}), \quad \Delta T = \frac{3T}{s \rho}\left(\frac{1}{r} - \frac{1}{R}\right)

Work done in changing surface area, and heat released when n identical droplets coalesce into a single large drop.

Examiner Tip: When droplets coalesce, surface area decreases, releasing energy and warming the liquid.

Top Examiner Traps & Pitfalls

Frequently tested misconceptions in Fluid Mechanics & Surface Tension

  • •Bernoulli's theorem applies ONLY to non-viscous, incompressible, irrotational streamline flow.
  • •Excess pressure in soap bubble has TWO surfaces: ΔP = 4T/R (liquid drop has only ONE surface: ΔP = 2T/R).