fluid-mechanics-expert

star 1

Expert-level fluid mechanics covering fluid statics, continuity, Bernoulli, Navier-Stokes, boundary layers, turbulence, pipe flow, and external aerodynamics.

luokai25 By luokai25 schedule Updated 4/11/2026

name: fluid-mechanics-expert version: 1.0.0 description: Expert-level fluid mechanics covering fluid statics, continuity, Bernoulli, Navier-Stokes, boundary layers, turbulence, pipe flow, and external aerodynamics. author: luo-kai tags: [fluid mechanics, Bernoulli, Navier-Stokes, turbulence, pipe flow, boundary layer]

Fluid Mechanics Expert

Before Starting

  1. Incompressible or compressible flow?
  2. Internal or external flow?
  3. Laminar or turbulent regime?

Core Expertise Areas

Fluid Statics

Pressure variation: dP over dz = negative rho g, increases with depth. Hydrostatic force: F = rho g h_c times A on submerged surface. Center of pressure: below centroid for inclined submerged surface. Buoyancy: upward force equals weight of displaced fluid.

Conservation Laws

Continuity: rho A V = constant for steady 1D flow. Bernoulli: P plus half rho V squared plus rho g z = constant along streamline. Momentum equation: sum of forces equals rate of change of momentum. Energy equation: adds shaft work and heat transfer to Bernoulli equation.

Viscous Flow

Reynolds number: Re = rho V L over mu, ratio of inertia to viscous forces. Laminar pipe flow: Poiseuille flow, parabolic velocity profile, f = 64 over Re. Turbulent pipe flow: Moody chart relates friction factor to Re and roughness. Navier-Stokes: governing equations for viscous flow, nonlinear, difficult to solve.

Boundary Layer

Boundary layer: thin region near wall where viscous effects important. Displacement thickness: effective thickness of zero velocity region. Transition: Re_x around 500,000 for flat plate boundary layer transition. Separation: adverse pressure gradient causes reverse flow and wake.

Turbulence

Reynolds averaging: separate mean and fluctuating components. Reynolds stresses: additional apparent stresses from turbulent fluctuations. k-epsilon model: two transport equations for turbulent kinetic energy and dissipation. DNS: direct numerical simulation resolves all scales, prohibitively expensive.

Best Practices

  • Check Reynolds number to determine flow regime before analysis
  • Verify Bernoulli assumptions before applying to problem
  • Use dimensional analysis to guide experimental design
  • Validate CFD results against analytical or experimental benchmarks

Common Pitfalls

Pitfall Fix
Applying Bernoulli across streamlines Bernoulli valid only along a streamline
Ignoring minor losses in pipe systems Include entrance, exit, fittings in head loss
Wrong turbulence model for separated flow Use more advanced model or LES for separated regions
Incorrect Reynolds number scaling Ensure dynamic similarity in experimental scaling

Related Skills

  • heat-transfer-expert
  • thermodynamics-mech-expert
  • physics/fluid-physics-expert
Install via CLI
npx skills add https://github.com/luokai25/luo_os-v_0.1 --skill fluid-mechanics-expert
Repository Details
star Stars 1
call_split Forks 0
navigation Branch main
article Path SKILL.md
More from Creator