Lesson 10.2 • Competency 10.2Complete Lesson
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Viscosity of Fluids & Stokes’ Law

Investigate internal fluid friction, Newton’s viscosity law F = η A (dv/dx), dynamic viscosity coefficient η, streamline and turbulent flow, Poiseuille’s pipe flow formula Q = (π P r⁴)/(8 η L), Stokes’ drag F_d = 6πηrv, and terminal velocity v_t.

Marking a lesson complete represents finishing your study of the topic; it does not denote tested mastery.

Learning Objectives

  • Define the coefficient of dynamic viscosity η and derive its SI unit (Pa·s or N·s·m⁻²).
  • State Stokes’ Law for a spherical body, explain its validity conditions, and derive the terminal velocity equation.
  • Apply Poiseuille’s equation to determine volume flow rate through cylindrical tubes under laminar conditions.

Core Theory & Concepts

Viscosity is internal fluid friction that resists relative motion between adjacent fluid layers. When a solid sphere moves slowly through a viscous fluid, viscous shear layers impart a drag force formulated by Sir George Gabriel Stokes as F_d = 6πηrv.

Stokes’ Drag Law

For a sphere of radius r moving at laminar speed v through a fluid of viscosity η: F_d = 6πηrv.

F_d = 6\pi \eta r v

Terminal Velocity Equation

When downward weight equals buoyant upthrust plus viscous drag, acceleration ceases and terminal velocity is attained.

v_t = \frac{2 r^2 (\rho - \sigma) g}{9 \eta}

Common Misconceptions

Misconception

Terminal velocity is directly proportional to sphere radius r.

Physical Clarification:Net gravitational driving force scales with volume (r³), while Stokes drag scales with (r·v). Thus terminal velocity scales with radius squared: v_t ∝ r².

Syllabus Topic Outline

Competency 10.2
  • 1Viscous shear resistance between adjacent laminar fluid layers
  • 2Newton’s law of viscosity: F = η A (dv/dx) and velocity gradient
  • 3Streamline versus turbulent flow and critical velocity
  • 4Poiseuille’s formula: Q = (π P r⁴) / (8 η L) and fourth-power radius dependence
  • 5Stokes’ Law: F_d = 6πηrv and terminal velocity derivation v_t = 2r²(ρ - σ)g / 9η
  • 6Stokes’ viscometer experimental design and wall effect precautions

Practice Problems

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Competency 10.2 • intermediate

Calculate the viscous drag force F_d in Newtons on a sphere of radius 2.0 mm falling at 0.050 m/s in oil of viscosity 0.80 Pa·s.

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