11.5 Dimensional Analysis, Similitude & Model Testing
Key Takeaways
- Dimensional analysis is named explicitly in the Fluid Mechanics bullet of the CIL Mechanical Paper-II syllabus.
- Buckingham's Pi theorem states that a relation among n variables involving m fundamental dimensions reduces to a relation among n minus m dimensionless groups.
- Reynolds number governs viscous-dominated flows such as pipe flow, while Froude number governs free-surface flows and Mach number governs compressible flows.
- Complete dynamic similarity requires geometric and kinematic similarity plus equality of the governing dimensionless number between model and prototype.
Why Dimensionless Groups Exist
The drag on a submerged body depends on its size, the fluid density and viscosity, and the velocity — five variables. Investigating that experimentally by varying each in turn would need an impractical number of tests. Dimensional analysis reduces the five variables to two dimensionless groups, so a single curve captures the entire relationship.
This is not merely a labour-saving device. It is also the reason a model tested in a laboratory can predict the behaviour of a full-size machine, and the reason correlations such as the Nusselt-Reynolds-Prandtl relations of heat transfer take the form they do.
Fundamental Dimensions
In the MLT system, every mechanical quantity reduces to mass $M$, length $L$ and time $T$.
| Quantity | Dimensions |
|---|---|
| Velocity | $LT^{-1}$ |
| Acceleration | $LT^{-2}$ |
| Force | $MLT^{-2}$ |
| Pressure, stress | $ML^{-1}T^{-2}$ |
| Density | $ML^{-3}$ |
| Dynamic viscosity $\mu$ | $ML^{-1}T^{-1}$ |
| Kinematic viscosity $\nu$ | $L^{2}T^{-1}$ |
| Surface tension | $MT^{-2}$ |
| Work, energy | $ML^{2}T^{-2}$ |
| Power | $ML^{2}T^{-3}$ |
| Momentum, impulse | $MLT^{-1}$ |
| Torque | $ML^{2}T^{-2}$ |
Note that torque and energy share dimensions but are physically distinct — dimensional identity does not imply physical equivalence.
Buckingham's Pi Theorem
If a physical problem involves $n$ variables and these contain $m$ fundamental dimensions, the relationship can be expressed in terms of $(n - m)$ independent dimensionless $\Pi$ groups.
Procedure
- List all $n$ variables and write their dimensions.
- Determine $m$, the number of fundamental dimensions present.
- Choose $m$ repeating variables. They must together contain all $m$ dimensions, must not themselves form a dimensionless group, and conventionally include one geometric variable (a length), one kinematic (a velocity) and one dynamic (density). The dependent variable must never be a repeating variable.
- Form $(n-m)$ groups, each consisting of the repeating variables raised to unknown powers multiplied by one non-repeating variable.
- Solve for the exponents by requiring each group to be dimensionless.
Worked example: drag force
Drag $F$ depends on velocity $v$, length $l$, density $\rho$ and viscosity $\mu$. Here $n = 5$ and $m = 3$, so there are $5 - 3 = 2$ groups.
Take $l$, $v$ and $\rho$ as repeating variables. The two groups turn out to be
So the general result is
which, written with the conventional factor of one half and area $A$, is exactly the familiar drag equation
Dimensional analysis has produced the form of the law without any experiment; experiment is needed only to find the function $f$.
The Principal Dimensionless Numbers
Each number is a ratio of inertia force to some other force, and each governs a different class of flow.
| Number | Definition | Ratio of | Governs |
|---|---|---|---|
| Reynolds $Re$ | $\dfrac{\rho v L}{\mu} = \dfrac{vL}{\nu}$ | Inertia to viscous | Pipe flow, submerged bodies, boundary layers |
| Froude $Fr$ | $\dfrac{v}{\sqrt{gL}}$ | Inertia to gravity | Free-surface flow: channels, spillways, ships |
| Euler $Eu$ | $\dfrac{v}{\sqrt{p/\rho}}$ | Inertia to pressure | Pressure-driven flow, cavitation |
| Weber $We$ | $\dfrac{\rho v^2 L}{\sigma}$ | Inertia to surface tension | Droplets, sprays, capillary waves, thin films |
| Mach $Ma$ | $\dfrac{v}{c}$ | Inertia to elastic | Compressible flow; $Ma > 0.3$ |
In heat transfer the same logic gives Nusselt, Prandtl, Grashof and Stanton numbers, which is why the two subjects share a methodology.
Critical values worth recalling
| Number | Threshold | Meaning |
|---|---|---|
| $Re$ in a pipe | 2000 / 4000 | Laminar below 2000; turbulent above 4000 |
| $Re$ on a flat plate | $5\times10^5$ | Transition to turbulent boundary layer |
| $Fr$ | 1 | Critical flow; below is subcritical, above is supercritical |
| $Ma$ | 1 | Sonic; below is subsonic, above supersonic |
| $Ma$ | 0.3 | Below this, flow may be treated as incompressible |
Similitude
For a model test to predict prototype behaviour, three conditions must hold in sequence.
1. Geometric similarity. The model is a true scale replica: every length ratio is the same, $L_r = L_m/L_p$. This includes surface roughness, which is often the hardest part to satisfy.
2. Kinematic similarity. Velocity and acceleration at corresponding points have the same ratio and the same direction. Streamline patterns are geometrically similar.
3. Dynamic similarity. Force ratios at corresponding points are equal. In practice this means making the governing dimensionless number equal in model and prototype.
All three are required; geometric similarity alone is not enough, and this hierarchy is a standard objective item.
Which number to match
| Flow situation | Match |
|---|---|
| Fully submerged body, closed pipe | Reynolds |
| Free surface present: ships, spillways, open channels | Froude |
| Compressible, high speed | Mach |
| Droplet formation, thin sheets | Weber |
It is generally impossible to satisfy Reynolds and Froude simultaneously with the same fluid. Froude similarity requires $v_r = \sqrt{L_r}$, while Reynolds similarity requires $v_r = 1/L_r$. For a 1:25 ship model, Froude gives $v_r = 0.2$ but Reynolds would demand $v_r = 25$. Naval architects resolve this by scaling on Froude for wave-making resistance and correcting the viscous friction component analytically — a genuine limitation of model testing rather than a mathematical curiosity.
Scale ratios under Froude similarity
With $L_r$ the length scale, matching Froude numbers gives:
| Quantity | Ratio |
|---|---|
| Velocity | $L_r^{1/2}$ |
| Time | $L_r^{1/2}$ |
| Acceleration | 1 |
| Discharge | $L_r^{5/2}$ |
| Force | $L_r^{3}$ |
| Power | $L_r^{7/2}$ |
Worked example
A spillway model is built to a scale of 1:36. If the model discharge is 0.5 m$^3$/s, find the prototype discharge.
A spillway has a free surface, so Froude similarity applies and $Q_r = L_r^{5/2}$. With $L_p/L_m = 36$:
Worked example: pipe flow
A 1:5 scale model of a mine ventilation duct is tested with the same air. Reynolds similarity requires $\rho v L/\mu$ to match, so with the same fluid
The model must be run at five times the prototype velocity — often impractical, which is why such models are frequently tested in water or in pressurised air to raise the density and bring the required velocity down.
Buckingham's Pi theorem states that a physical relationship among n variables containing m fundamental dimensions can be reduced to a relationship among:
For model testing of a spillway, where a free surface is present, dynamic similarity is achieved by matching the:
The Reynolds number represents the ratio of:
A spillway model is built to a scale of 1:36 and discharges 0.5 cubic metres per second. The corresponding prototype discharge is: