Displacement Thickness and Momentum Thickness Calculator

Find the Blasius displacement thickness, momentum thickness, and shape factor for laminar flow over a flat plate.

📊 Displacement Thickness and Momentum Thickness Calculator
Distance from leading edge (x)0.3
m
0.015
m/s
kg/m³
Pa·s
Displacement Thickness δ* (mm)
Momentum Thickness θ (mm)
Shape Factor H
Boundary Layer Thickness δ (mm)
Local Reynolds Number Re_x
Flow Regime
Step-by-step working

📊 What is the Displacement Thickness and Momentum Thickness Calculator?

This displacement thickness and momentum thickness calculator uses the Blasius solution to find two boundary layer measures that matter more for engineering purposes than the raw 99% thickness delta. Enter the free-stream velocity U, the distance from the leading edge x, the fluid density rho, and the dynamic viscosity mu, and it returns displacement thickness delta*, momentum thickness theta, the shape factor H, the 99% thickness delta for reference, the local Reynolds number Re_x, and a chart of both thicknesses growing along the plate.

Displacement thickness delta* is the distance the outer inviscid flow is effectively displaced outward because the slower-moving fluid near the wall carries less mass than an equivalent slice of free-stream flow. It matters directly for sizing wind tunnel test sections, duct and nozzle inlets, and any design where the effective outer shape seen by the main flow needs to account for the boundary layer. Momentum thickness theta measures the momentum deficit in the boundary layer, and it connects directly to skin friction drag through the momentum integral equation, making it the preferred quantity for computing total viscous drag on a flat plate or airfoil surface.

A common misconception is that delta*, theta, and the 99% thickness delta are roughly the same size, they are not. For a Blasius laminar boundary layer, theta is the smallest, delta* sits in the middle at about a third of delta, and delta is the largest. Another important distinction: the shape factor H = delta*/theta is a fixed 2.5916 for laminar Blasius flow, so tracking how H drifts away from that value in real (non-idealized) boundary layer data is a standard way engineers detect an adverse pressure gradient pushing the flow toward separation.

This calculator is a quick reference for aerodynamics and fluid mechanics coursework, boundary layer displacement and momentum calculations for wind tunnel and duct design, and sanity-checking CFD results against the exact laminar flat-plate solution.

📐 Formula

Re_x  =  ρUx / μ
ρ = fluid density (kg/m³)
U = free-stream velocity (m/s)
x = distance from the leading edge (m)
μ = dynamic viscosity (Pa·s)
δ*  =  1.7208x / √Re_x      θ  =  0.664x / √Re_x
δ* = displacement thickness (m), the mass-flow-deficit measure
θ = momentum thickness (m), the momentum-deficit measure
Example: U = 10 m/s, x = 0.3 m, air (ρ = 1.225 kg/m³, μ = 1.81×10⁻⁵ Pa·s), Re_x ≈ 2.0304×10&sup5;, δ* ≈ 1.146 mm, θ ≈ 0.442 mm.
H  =  δ* / θ      δ (reference)  =  5.0x / √Re_x
H = shape factor (dimensionless), always 1.7208/0.664 = 2.5916 for Blasius laminar flow, a useful consistency check
δ = 99% boundary layer thickness (m), included for comparison against δ* and θ

📖 How to Use This Calculator

Steps

1
Enter the distance from the leading edge. Use the slider or type the distance x, in metres, measured from the front edge of the flat plate.
2
Enter the free-stream velocity, density, and viscosity. Enter U in m/s, fluid density rho in kg/m3, and dynamic viscosity mu in Pa.s.
3
Read the displacement and momentum thickness results and chart. See delta*, theta, H, delta, Re_x, the flow regime label, and the delta* versus theta versus x chart.

💡 Example Calculations

Example 1 - Air over a small lab-scale plate (default values)

1
U = 10 m/s, x = 0.3 m, air at ρ = 1.225 kg/m³, μ = 1.81×10⁻⁵ Pa·s
2
Re_x = 1.225 × 10 × 0.3 ÷ 0.0000181 = 2.0304×10&sup5;, this is below 5×10&sup5;, so the flow is laminar
3
δ* = 1.7208 × 0.3 ÷ √203038.674 = 1.146 mm, θ = 0.664 × 0.3 ÷ √203038.674 = 0.442 mm, H = 1.146 ÷ 0.442 = 2.5916, δ (reference) = 3.329 mm
δ* = 1.146 mm, θ = 0.442 mm, H = 2.5916, Laminar
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Example 2 - Air over a longer plate at lower speed

1
U = 5 m/s, x = 0.8 m, air at ρ = 1.225 kg/m³, μ = 1.81×10⁻⁵ Pa·s
2
Re_x = 1.225 × 5 × 0.8 ÷ 0.0000181 = 2.7072×10&sup5;, still below 5×10&sup5;, so the flow is laminar
3
δ* = 1.7208 × 0.8 ÷ √270718.232 = 2.646 mm, θ = 0.664 × 0.8 ÷ √270718.232 = 1.021 mm, H = 2.646 ÷ 1.021 = 2.5916, δ (reference) = 7.688 mm
δ* = 2.646 mm, θ = 1.021 mm, H = 2.5916, Laminar
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Example 3 - Water flow, turbulent-transition regime

1
U = 2 m/s, x = 1 m, water at ρ = 1000 kg/m³, μ = 0.001 Pa·s
2
Re_x = 1000 × 2 × 1 ÷ 0.001 = 2.0000×10&sup6;, this is above 5×10&sup5;, so Blasius laminar theory no longer applies here
3
The calculator still returns δ* = 1.217 mm and θ = 0.470 mm from the laminar formulas, H = 2.5916 (the invariant still holds since it is a pure ratio of constants), but flags the result as turbulent-transition, meaning turbulent correlations should be used for the real thicknesses instead
δ* = 1.217 mm (laminar formula only), θ = 0.470 mm, Re_x = 2.0000×10&sup6;, Turbulent (Blasius invalid)
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Example 4 - Invalid input: zero distance from the leading edge

1
x = 0 m (at the leading edge itself), U = 10 m/s, air
2
A boundary layer has not yet formed at x = 0, and the formulas divide by a Reynolds number of zero. The calculator shows an error instead of a result.
Error: distance from the leading edge x must be greater than 0
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❓ Frequently Asked Questions

What is displacement thickness in a boundary layer?+
Displacement thickness (delta*) is the distance the outer inviscid flow is effectively pushed outward, away from the wall, because the slower-moving fluid inside the boundary layer carries less mass than an equivalent layer of free-stream flow. For the Blasius solution, delta* = 1.7208x / sqrt(Re_x).
What is momentum thickness in a boundary layer?+
Momentum thickness (theta) measures the momentum deficit in the boundary layer compared to free-stream flow, and it is directly related to skin friction drag on a flat plate. For the Blasius solution, theta = 0.664x / sqrt(Re_x), the same 0.664 that appears in the local skin friction coefficient formula.
What is the shape factor H and why does it matter?+
The shape factor H = delta*/theta describes the general shape of the boundary layer velocity profile. For a Blasius laminar boundary layer H is always 2.5916, a fixed invariant. In real flows, H rising well above 2.6 signals the boundary layer is approaching separation under an adverse pressure gradient, while a falling H is typical of the transition to turbulence.
How is displacement thickness different from the 99% boundary layer thickness delta?+
The 99% thickness delta marks where velocity reaches 99% of free-stream U, while displacement thickness delta* is a mass-flow-deficit integral over the whole profile. For a Blasius boundary layer delta* is only about 1.7208/5.0, roughly 34%, of delta, since most of the mass deficit sits close to the wall.
Why is momentum thickness theta always the smallest of the three thickness measures?+
Momentum thickness weights the velocity deficit by the local velocity itself, so its integral is concentrated in the thin region very near the wall where both the deficit and the local velocity are significant. This makes theta smaller than displacement thickness delta*, which in turn is smaller than the 99% thickness delta.
What is the local Reynolds number Re_x used in these formulas?+
Re_x = rho U x / mu, where rho is fluid density, U is free-stream velocity, x is distance from the leading edge, and mu is dynamic viscosity. It is called 'local' because it changes with position x along the plate, and it is the single number that sets delta, delta*, theta, and H at that station.
When do these Blasius formulas stop being valid?+
The Blasius formulas for delta*, theta, and H assume laminar flow, which holds until the local Reynolds number Re_x reaches roughly 5x10^5, the classic transition value for a flat plate. Past that point the boundary layer becomes turbulent and different, higher-value correlations for delta* and theta apply instead.
Do I need kinematic viscosity or dynamic viscosity for this calculator?+
This calculator takes fluid density (rho) and dynamic viscosity (mu) as separate inputs, matching how most textbooks and material property tables present the data. Kinematic viscosity, if you have it instead, is nu = mu / rho, so multiply nu by rho to recover mu before entering it.
How are displacement thickness and momentum thickness used in drag calculations?+
Momentum thickness theta is directly proportional to the local skin friction drag on a flat plate through the momentum integral equation, so it is the preferred thickness measure for computing total viscous drag. Displacement thickness delta* is instead used to correct the effective shape seen by the outer inviscid flow, for example when sizing wind tunnel test sections or duct inlets.
What are typical displacement and momentum thickness values in practice?+
For air at 10 m/s flowing 0.3 m from the leading edge of a flat plate, the Blasius displacement thickness delta* is about 1.146 mm and the momentum thickness theta is about 0.442 mm, both a fraction of a millimetre, which shows how thin these boundary layer measures are at everyday lab-scale speeds and distances.
Does the shape factor H change with fluid type or speed for laminar flow?+
No. Because H = delta*/theta = 1.7208/0.664 comes directly from dividing two constants in the Blasius similarity solution, it always equals 2.5916 for laminar flow regardless of the fluid density, viscosity, velocity, or position x. H only changes once the flow leaves the laminar Blasius regime.

What is displacement thickness in a boundary layer?

Displacement thickness (delta*) is the distance the outer inviscid flow is effectively pushed outward, away from the wall, because the slower-moving fluid inside the boundary layer carries less mass than an equivalent layer of free-stream flow. For the Blasius solution, delta* = 1.7208x / sqrt(Re_x).

What is momentum thickness in a boundary layer?

Momentum thickness (theta) measures the momentum deficit in the boundary layer compared to free-stream flow, and it is directly related to skin friction drag on a flat plate. For the Blasius solution, theta = 0.664x / sqrt(Re_x), the same 0.664 that appears in the local skin friction coefficient formula.

What is the shape factor H and why does it matter?

The shape factor H = delta*/theta describes the general shape of the boundary layer velocity profile. For a Blasius laminar boundary layer H is always 2.5916, a fixed invariant. In real flows, H rising well above 2.6 signals the boundary layer is approaching separation under an adverse pressure gradient, while a falling H is typical of the transition to turbulence.

How is displacement thickness different from the 99% boundary layer thickness delta?

The 99% thickness delta marks where velocity reaches 99% of free-stream U, while displacement thickness delta* is a mass-flow-deficit integral over the whole profile. For a Blasius boundary layer delta* is only about 1.7208/5.0, roughly 34%, of delta, since most of the mass deficit sits close to the wall.

Why is momentum thickness theta always the smallest of the three thickness measures?

Momentum thickness weights the velocity deficit by the local velocity itself, so its integral is concentrated in the thin region very near the wall where both the deficit and the local velocity are significant. This makes theta smaller than displacement thickness delta*, which in turn is smaller than the 99% thickness delta.

What is the local Reynolds number Re_x used in these formulas?

Re_x = rho U x / mu, where rho is fluid density, U is free-stream velocity, x is distance from the leading edge, and mu is dynamic viscosity. It is called 'local' because it changes with position x along the plate, and it is the single number that sets delta, delta*, theta, and H at that station.

When do these Blasius formulas stop being valid?

The Blasius formulas for delta*, theta, and H assume laminar flow, which holds until the local Reynolds number Re_x reaches roughly 5x10^5, the classic transition value for a flat plate. Past that point the boundary layer becomes turbulent and different, higher-value correlations for delta* and theta apply instead.

Do I need kinematic viscosity or dynamic viscosity for this calculator?

This calculator takes fluid density (rho) and dynamic viscosity (mu) as separate inputs, matching how most textbooks and material property tables present the data. Kinematic viscosity, if you have it instead, is nu = mu / rho, so multiply nu by rho to recover mu before entering it.

How are displacement thickness and momentum thickness used in drag calculations?

Momentum thickness theta is directly proportional to the local skin friction drag on a flat plate through the momentum integral equation, so it is the preferred thickness measure for computing total viscous drag. Displacement thickness delta* is instead used to correct the effective shape seen by the outer inviscid flow, for example when sizing wind tunnel test sections or duct inlets.

What are typical displacement and momentum thickness values in practice?

For air at 10 m/s flowing 0.3 m from the leading edge of a flat plate, the Blasius displacement thickness delta* is about 1.146 mm and the momentum thickness theta is about 0.442 mm, both a fraction of a millimetre, which shows how thin these boundary layer measures are at everyday lab-scale speeds and distances.

Does the shape factor H change with fluid type or speed for laminar flow?

No. Because H = delta*/theta = 1.7208/0.664 comes directly from dividing two constants in the Blasius similarity solution, it always equals 2.5916 for laminar flow regardless of the fluid density, viscosity, velocity, or position x. H only changes once the flow leaves the laminar Blasius regime.