Physic Labs

Fluid mechanics

Viscosity and the Reynolds number

Viscosity describes internal friction in a fluid; the Reynolds number compares inertial and viscous effects to characterize flow regimes.

Real fluids resist shear through viscosity. Flow is often laminar at low Reynolds number; when inertia is more dominant, fluctuations and turbulent mixing can develop.

Re=ρvLμ=vLν,τ=μ∂u∂yRe=\frac{\rho vL}{\mu}=\frac{vL}{\nu},\qquad \tau=\mu\frac{\partial u}{\partial y}

Definition: Dynamic viscosity

Dynamic viscosity μ\mu (Pa·s) relates shear stress to velocity gradient; kinematic viscosity is ν=μ/ρ\nu=\mu/\rho (m²/s). LL and vv are characteristic length and speed.

Vary Reynolds number to explore qualitative flow changes; the parabolic profile represents laminar Poiseuille flow in a circular pipe.

Pipe-flow regimes

In a straight circular pipe, low ReRe generally favors laminar flow. Transition depends on disturbances and inlet conditions; Re≈2300Re\approx2300 is a common practical guide, not an exact universal threshold. At high ReRe, inertia can sustain fluctuations and turbulent mixing.

Poiseuille profile

u(r)=Δp4μℓ(R2−r2),Q=πR4Δp8μℓu(r)=\frac{\Delta p}{4\mu\ell}(R^2-r^2),\qquad Q=\frac{\pi R^4\Delta p}{8\mu\ell}

Fully developed laminar flow of a Newtonian liquid in a circular pipe has a parabolic profile: velocity is zero at the wall (no slip) and maximal on the axis. Poiseuille’s formula requires laminar flow and suitable pipe assumptions.

Example: Estimating Reynolds number

Water (ρ=1000 kg/m3\rho=1000\,\mathrm{kg/m^3}, μ=0.001 Pa s\mu=0.001\,\mathrm{Pa\,s}) flows at v=0.20 m/sv=0.20\,\mathrm{m/s} in a pipe of diameter D=0.010 mD=0.010\,\mathrm m. Find ReRe.

Solution

Re=ρvD/μ=1000(0.20)(0.010)/0.001=2000Re=\rho vD/\mu=1000(0.20)(0.010)/0.001=2000. This is often laminar in a smooth pipe, though disturbances still affect transition.

Quick check

Example: Estimating Reynolds number in a pipe

Water with ho=1000,mathrmkg/m3 ho=1000,mathrm{kg/m^3} and mu=1.0imes10−3,mathrmPa,smu=1.0 imes10^{-3},mathrm{Pa,s} flows through a pipe of diameter D=0.020,mathrmmD=0.020,mathrm m at mean speed v=0.10,mathrmm/sv=0.10,mathrm{m/s}. Then Re=hovD/mu=2000Re= ho vD/mu=2000. This is near the commonly observed transition range in a circular pipe, so inlet disturbances and roughness can determine whether flow remains laminar or becomes unstable; a single threshold is not an absolute boundary.

If ReRe rises because speed increases, which effect becomes relatively stronger?

Where is speed maximal in laminar Poiseuille flow?

References

  1. Frank M. White (2016). Fluid Mechanics