Fluid Dynamics Notes

This note is adapted from course materials for MNE3122 Fluid Mechanics and MNE4201 Aerodynamics at City University of Hong Kong. Instructors: course teaching staff.

Central Question

How do mass, momentum, energy, viscosity, pressure, vorticity, compressibility, and boundaries determine how fluids move and what forces they exert?

Fluid dynamics is conservation law plus regime judgment. The same equations cover creeping microflows, pipe networks, aircraft wings, blood flow, pumps, weather, nozzles, and shocks, but different terms dominate in different regimes.

\[\text{system boundary} \rightarrow \text{conservation laws} \rightarrow \text{dimensionless groups} \rightarrow \text{dominant balances} \rightarrow \text{models/correlations} \rightarrow \text{forces, losses, and validation}.\]
Fluid model hierarchy from conservation laws to inviscid viscous incompressible compressible laminar turbulent and CFD models
Figure 1. Fluid-model hierarchy. Conservation laws are universal, but regime assumptions decide whether Bernoulli, pipe correlations, boundary-layer theory, CFD, or compressible-flow relations are appropriate.

1. Conservation Laws

Mass conservation is

\[\frac{\partial \rho}{\partial t}+\nabla\cdot(\rho\mathbf{u})=0.\]

For incompressible flow, (\rho=\text{constant}), so

\[\nabla\cdot\mathbf{u}=0.\]

Momentum conservation for a Newtonian incompressible fluid with constant viscosity is

\[\rho\left(\frac{\partial\mathbf{u}}{\partial t}+\mathbf{u}\cdot\nabla\mathbf{u}\right) =-\nabla p+\mu\nabla^2\mathbf{u}+\rho\mathbf{g}.\]

Energy becomes necessary when temperature, compressibility, combustion, or heat transfer matters:

\[\rho c_p\left(\frac{\partial T}{\partial t}+\mathbf{u}\cdot\nabla T\right) =k\nabla^2T+\Phi+\dot q'''.\]

The nonlinear convective acceleration term (\mathbf{u}\cdot\nabla\mathbf{u}) is why exact solutions are rare and why turbulence, separation, and vortex shedding are hard.


2. Regime Selection

Dimensionless groups tell us which physics dominates:

Group Formula Meaning
Reynolds (Re=\rho UL/\mu) inertia / viscosity
Mach (Ma=U/a) speed / acoustic speed
Froude (Fr=U/\sqrt{gL}) inertia / gravity
Prandtl (Pr=\nu/\alpha) momentum diffusion / heat diffusion
Peclet (Pe=RePr) advection / heat diffusion
Strouhal (St=fL/U) unsteadiness / convection
Fluid regime map using Reynolds and Mach number to classify creeping laminar turbulent incompressible and compressible flows
Figure 2. Fluid regime map. Reynolds and Mach numbers are often the first split: viscous versus inertial, incompressible versus compressible.

Regime mistakes are expensive. Bernoulli fails in separated, highly viscous, or strongly unsteady regions. Incompressible models fail when density variation matters. Laminar correlations fail in turbulence. CFD fails when the boundary conditions or turbulence model are wrong.


3. Statics, Bernoulli, and Mechanical Energy

For a fluid at rest,

\[\frac{dp}{dz}=-\rho g, \qquad p=p_0+\rho gh\]

for constant-density liquids. Buoyancy is

\[F_B=\rho_f g V_{\text{displaced}}.\]

For steady, incompressible, inviscid flow along a streamline,

\[\frac{p}{\rho g}+\frac{V^2}{2g}+z=\text{constant}.\]

Real pipe systems add machines and losses:

\[\frac{p_1}{\rho g}+\alpha_1\frac{V_1^2}{2g}+z_1+h_p = \frac{p_2}{\rho g}+\alpha_2\frac{V_2^2}{2g}+z_2+h_t+h_L.\]

Bernoulli is not a magic pressure-speed slogan. It is mechanical energy conservation under restrictive assumptions.


4. Viscous Flow, Boundary Layers, and Losses

Viscosity diffuses momentum. At high (Re), viscosity may be negligible in the outer flow but remains decisive near walls and in wakes.

Boundary layer diagram showing wall velocity profile growth adverse pressure gradient separation and wake
Figure 3. Boundary-layer logic. Viscosity is concentrated near walls; adverse pressure gradients can reverse near-wall flow and cause separation.

Pipe losses are commonly represented by Darcy-Weisbach:

\[h_f=f\frac{L}{D}\frac{V^2}{2g}.\]

The friction factor (f) depends on Reynolds number and relative roughness. Minor losses from bends, valves, entrances, and exits are often written

\[h_m=K\frac{V^2}{2g}.\]

The engineering task is to account for all relevant loss mechanisms without pretending correlations are universal constants.


5. Lift, Drag, and Aerodynamics

Aerodynamic forces are usually nondimensionalized:

\[C_L=\frac{L}{\frac12\rho V^2S}, \qquad C_D=\frac{D}{\frac12\rho V^2S}.\]

Lift comes from pressure and shear integrated over the body, not from one isolated story. Circulation, pressure field, angle of attack, boundary-layer state, and separation all matter.

Drag includes:

Stall occurs when adverse pressure gradient and separation destroy the attached-flow lift mechanism. Airfoil data are therefore regime data: Reynolds number, Mach number, surface roughness, and turbulence level matter.


6. Compressible Flow, Shocks, and Nozzles

Compressibility matters when density changes couple to motion, often for (Ma\gtrsim0.3). The speed of sound for an ideal gas is

\[a=\sqrt{\gamma RT}.\]

For isentropic ideal-gas flow,

\[\frac{T_0}{T}=1+\frac{\gamma-1}{2}Ma^2.\]

Nozzles reveal the key compressible-flow surprise: a converging-diverging nozzle accelerates subsonic flow in the converging part, reaches (Ma=1) at the throat if choked, and accelerates supersonically in the diverging part.

Converging diverging nozzle diagram showing subsonic throat choking supersonic expansion normal shock and pressure ratio
Figure 4. Compressible nozzle logic. Choking, expansion, and shocks depend on pressure ratio and geometry.

Shocks are thin irreversible compression waves. Across a shock, pressure, temperature, density, and entropy rise, while Mach number drops. Shocks are not numerical artifacts; they are physical consequences of compressible nonlinear conservation laws.


7. CFD and Experimental Validation

CFD solves discretized conservation laws. It is powerful only when the model choices match the flow:

Fluid validation loop linking regime analysis hand estimates CFD experiment conservation residuals and design decision
Figure 5. Fluid validation loop. Regime analysis, reduced models, CFD, experiments, and residual checks should constrain one another.

Good fluid engineering triangulates: hand estimates set scale, CFD resolves fields, experiments reveal reality, and conservation checks catch nonsense.


What This Framework Lets Us Do

It lets us choose the right simplification: hydrostatics for rest, Bernoulli for ideal mechanical energy, pipe correlations for internal viscous losses, boundary-layer theory for wall effects, compressible relations for high Mach, and CFD when geometry/regime complexity requires field simulation.

Where the Framework Stops Being Reliable

It fails when regime assumptions are wrong: high (Ma) treated incompressibly, separated flow treated inviscid, turbulence treated laminar, cavitation ignored, multiphase flow simplified as single-phase, or CFD used without validation.

Where the Subject Leads Next

Fluid dynamics leads to aerodynamics, turbomachinery, combustion, heat transfer, ocean/atmospheric flows, biomedical flows, CFD, and flow control.


Technical and Editorial Audit

Area Correction or decision
Central question Reframed fluid dynamics around conservation laws and regime selection.
Preserved equations Kept continuity, Navier-Stokes, energy, hydrostatics, Bernoulli, pipe losses, lift/drag coefficients, speed of sound, and isentropic stagnation relation.
Figures Added five original SVG diagrams for model hierarchy, regime map, boundary layer separation, nozzle/shock logic, and validation loop.
Key correction Emphasized assumptions behind Bernoulli, correlations, compressibility thresholds, and CFD.

Main Sources Used in This Note