NEET · Physics

NEET Properties of Solids and Liquids: Elasticity, Fluids, Viscosity and Surface Tension

Own the mechanical solids-and-fluids portion of official Unit 7: elasticity, fluid pressure, Pascal law, viscosity, Stokes/terminal velocity, streamline/turbulent flow, Bernoulli and surface tension/capillarity. Thermal content is carved out to Thermal Properties.

Subject
Physics
Official syllabus unit
Unit 7: Properties of Solids and Liquids

In short

This Rank Sarthi route owns the mechanical part of official Unit 7. It covers stress-strain and elastic moduli, fluid pressure and Pascal law, viscosity and terminal velocity, flow/Bernoulli relationships, surface tension, excess pressure and capillary rise. Temperature, expansion, calorimetry, phase change and heat transfer belong to Thermal Properties.

Subject faculty

Ashwini M., Physics Expert at Rank Sarthi

Ashwini M.

Physics Expert

Physics • NEET

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Also in Physics: Kumar Gandharva Saxena

Syllabus mapping

  • Unit
    Focused part of a larger current official unit
    Topics
    Solids: deformation and elasticity, Fluids at rest, Viscous flow, Flow energy and surface phenomena, Thermal carve-out

Before this chapter

Concepts in this chapter

1. Solids: deformation and elasticity

Stress describes applied force per area; strain describes relative deformation. In the linear elastic region, modulus ratios relate stress to strain. Hooke-law language must remain inside the regime where stress is proportional to strain.

2. Fluids at rest

Pressure in a fluid acts normally to surfaces. Hydrostatic pressure change follows density, gravity and depth in the simple constant-density model. Pascal's principle describes pressure transmission in a confined fluid and supports hydraulic applications.

3. Viscous flow

Viscosity describes internal resistance to relative motion in fluid layers. Stokes' drag and the familiar terminal-speed formula apply to a small sphere in the low-Reynolds-number/laminar regime with the associated idealizations. They are not universal drag laws.

4. Flow energy and surface phenomena

Bernoulli's relation applies along a streamline for an ideal steady incompressible non-viscous flow model. Surface tension acts tangentially along a liquid surface and creates pressure differences across curved interfaces. Drop and soap-bubble formulas differ because a soap bubble has two liquid-air surfaces.

5. Thermal carve-out

Official Unit 7 continues into heat, temperature, thermal expansion, specific heat, calorimetry, phase change and heat transfer. Those relationships belong to /neet/physics/thermal-properties so this page does not duplicate them.

6. Decision aids for this chapter

  • Unit 7 split diagram: mechanical vs thermal ownership
  • Stokes-regime condition card
  • Drop vs bubble surface-count graphic

Formula sheet

  • Normal stress: σ = F_perp/A. Pa = N m^-2. Scalar magnitude for simple normal loading; sign convention should be stated if tension/compression signs are used.

    Normal stress

    Use when — Pa = N m^-2. Scalar magnitude for simple normal loading; sign convention should be stated if tension/compression signs are used.

  • Longitudinal strain: ε = ΔL/L. Dimensionless; small-deformation model.

    Longitudinal strain

    Use when — Dimensionless; small-deformation model.

  • Young modulus: Y = stress/longitudinal strain. Pa. Linear elastic region only.

    Young modulus

    Use when — Pa. Linear elastic region only.

  • Bulk modulus: B = -ΔP/(ΔV/V). Pa. Minus sign reflects decrease in volume for positive pressure increase under the common convention.

    Bulk modulus

    Use when — Pa. Minus sign reflects decrease in volume for positive pressure increase under the common convention.

  • Hydrostatic pressure difference: ΔP = ρ g h. Pa. Constant-density fluid, uniform g, depth difference h.

    Hydrostatic pressure difference

    Use when — Pa. Constant-density fluid, uniform g, depth difference h.

  • Stokes drag: F_d = 6πηrv. N. Sphere of radius r moving slowly in viscous fluid; low-Reynolds-number Stokes regime.

    Stokes drag

    Use when — N. Sphere of radius r moving slowly in viscous fluid; low-Reynolds-number Stokes regime.

  • Terminal speed sphere: v_t = 2r^2(ρ_s-ρ_f)g/(9η). m s^-1. Small sphere, Stokes regime, steady terminal motion, buoyancy included, ρ_s>ρ_f for downward terminal fall.

    Terminal speed sphere

    Use when — m s^-1. Small sphere, Stokes regime, steady terminal motion, buoyancy included, ρ_s>ρ_f for downward terminal fall.

  • Bernoulli: P + (1/2)ρv^2 + ρgh = constant. Energy per volume; steady incompressible non-viscous flow along a streamline under gravity.

    Bernoulli

    Use when — Energy per volume; steady incompressible non-viscous flow along a streamline under gravity.

  • Excess pressure drop: ΔP = 2T/r. Single spherical liquid-air interface, e.g. droplet; T N m^-1.

    Excess pressure drop

    Use when — Single spherical liquid-air interface, e.g. droplet; T N m^-1.

  • Excess pressure soap bubble: ΔP = 4T/r. Soap bubble with two surfaces.

    Excess pressure soap bubble

    Use when — Soap bubble with two surfaces.

  • Capillary rise/depression: h = 2T cosθ/(ρ g r). Circular capillary of radius r; static equilibrium and ideal wetting geometry; sign follows cosθ.

    Capillary rise/depression

    Use when — Circular capillary of radius r; static equilibrium and ideal wetting geometry; sign follows cosθ.

Worked examples

A small sphere falls through the same viscous liquid under Stokes conditions. If its radius doubles while density difference and viscosity stay the same, how does terminal speed change?

Concept being tested: Stokes terminal speed

Prompt: A small sphere falls through the same viscous liquid under Stokes conditions. If its radius doubles while density difference and viscosity stay the same, how does terminal speed change?

Decisive condition: The terminal-speed formula under the stated model has v_t ∝ r^2.

Method choice: Use the ratio (2r)^2/r^2.

Reasoning/calculation: Terminal speed becomes 4 times the original value.

Unit/sign/condition check: The conclusion is dimensionless ratio; it is valid only while both cases remain in the Stokes regime and other parameters are unchanged.

PI if answered incorrectly: Decision / Selection Error if the proportionality is used outside the model conditions.

Common mistakes and what they actually indicate

  • Using f=6πηrv at high-speed/turbulent conditions

    Decision / selection error

    Why it happens

    Preparation Intelligence classification: Decision / Selection Error.

    How it is corrected

    Check the Stokes/low-Reynolds model.

  • Using 2T/r for a soap bubble

    Recall gap

    Why it happens

    Preparation Intelligence classification: Recall Gap.

    How it is corrected

    A soap bubble has two surfaces, giving 4T/r.

  • Applying Bernoulli despite strong viscosity/energy loss without qualification

    Decision / selection error

    Why it happens

    Preparation Intelligence classification: Decision / Selection Error.

    How it is corrected

    Check the ideal steady-flow assumptions.

  • Treating Hooke behavior as valid beyond the linear elastic range

    Knowledge gap

    Why it happens

    Preparation Intelligence classification: Knowledge Gap.

    How it is corrected

    State the linear-region condition.

FAQ

NEET Properties of Solids and Liquids: Elasticity, Fluids, Viscosity and Surface Tension — questions

Straight answers about how Rank Sarthi fits into serious exam preparation.

The mechanical solids-and-fluids portion of official Unit 7.

Sources and provenance

Official scope is taken from the NEET (UG) 2026 syllabus and official NTA documents; concept structure follows current NCERT contents. No performance, weightage or question-frequency data is asserted.