This laminar flow rate calculator uses the Hagen–Poiseuille equation to estimate the volumetric flow rate of a Newtonian fluid through a straight, circular pipe. By entering the pressure drop, pipe radius, fluid viscosity, and pipe length, you can quickly determine how much fluid flows per unit time under laminar conditions.
The tool is aimed at students, technicians, and engineers working with small pipes and tubes, microfluidic channels, or other low-Reynolds-number systems where viscous effects dominate and flow is smooth and orderly. The calculator assumes fully developed, incompressible, laminar flow in a rigid circular pipe with constant radius.
Fluid flow in pipes is often classified as either laminar or turbulent. In laminar flow, fluid moves in parallel layers with minimal mixing between them. Velocity is highest at the center of the pipe and decreases smoothly to zero at the pipe wall. This behavior makes the relationship between pressure drop and flow rate predictable and linear.
In contrast, turbulent flow is characterized by swirling eddies and chaotic motion. Under turbulent conditions, energy losses increase significantly and the simple Hagen–Poiseuille equation no longer applies. Instead, more complex correlations and friction-factor charts are needed.
The most common way to distinguish laminar from turbulent flow in a circular pipe is the Reynolds number, defined as:
Re = (ρ · v · D) / μ
where ρ is fluid density, v is average velocity, D is pipe diameter, and μ is dynamic viscosity. For flow in a smooth, circular tube:
The Hagen–Poiseuille equation, and therefore this calculator, is intended only for the laminar regime.
The Hagen–Poiseuille equation gives the volumetric flow rate Q of a Newtonian fluid through a long, straight, circular pipe under steady, laminar conditions:
Text form:
Q = (π · ΔP · r4) / (8 · μ · L)
where:
In mathematical markup, the same relationship can be expressed as:
The radius term appears to the fourth power. This strong dependence means that even small changes in radius can dramatically affect flow rate: for example, doubling the radius increases flow by a factor of 16, all else equal.
To use the calculator correctly, pay close attention to both units and the distinction between radius and diameter.
Pressure drop ΔP (Pa)
Enter the pressure difference between the inlet and outlet measurement points along the pipe in pascals (Pa). If your data are in kilopascals (kPa) or bar, convert them first:
Pipe radius r (m)
Enter the inner radius of the pipe in meters. If you know the diameter D, compute r = D / 2. For example, a tube with inner diameter of 4 mm has a radius of 0.002 m. Always convert millimeters or centimeters to meters before entering the value.
Fluid viscosity μ (Pa·s)
Enter the dynamic viscosity in pascal-seconds (Pa·s). Typical values at room temperature include:
Check a reliable reference or data sheet for your specific fluid and temperature.
Pipe length L (m)
Enter the length between the two pressure measurement points in meters. For example, 50 cm of tubing corresponds to L = 0.5 m.
Compute and read the result
After entering all four values, run the calculation. The tool will return Q in cubic meters per second (m³/s). You can convert the result to other units if needed, such as liters per minute (L/min) or milliliters per minute (mL/min).
The calculator outputs the volumetric flow rate Q in m³/s. Depending on the magnitude of the result, it is often convenient to convert to more familiar units:
Because the Hagen–Poiseuille equation assumes laminar flow, the numerical result should be interpreted as an ideal prediction under those conditions. Real systems may deviate due to entrance effects, fittings, slight pipe roughness, or minor temperature changes that alter viscosity.
If you have an estimate of fluid density and pipe diameter, you can back-calculate the average velocity v from the volumetric flow rate Q using:
v = Q / A = Q / (π r²)
Once v is known, you can compute Reynolds number to confirm that laminar assumptions are valid. If the resulting Reynolds number is well below 2 000, the prediction from the calculator is more likely to be accurate.
Consider water at room temperature flowing through a small plastic tube. Assume:
Apply the Hagen–Poiseuille equation:
Q = (π · ΔP · r4) / (8 · μ · L)
Compute r4:
r = 0.001 m → r4 = (0.001)4 = 10−12 m4
Substitute all values:
Q = [π · 2 000 · 10−12] / [8 · 0.001 · 0.5]
The numerator is:
π · 2 000 · 10−12 ≈ 6.283 × 10−9
The denominator is:
8 · 0.001 · 0.5 = 0.004
Therefore:
Q ≈ (6.283 × 10−9) / 0.004 ≈ 1.57 × 10−6 m³/s
This corresponds to about 1.57 mL/s, or roughly 94 mL/min. This magnitude is typical for laminar flow through a 2 mm inner diameter tube at modest pressure drop.
If you then calculate the average velocity v using v = Q / (π r²), you can estimate the Reynolds number and verify that laminar conditions hold for this example.
The table below summarizes some key differences between laminar and turbulent flow in pipes and highlights when the Hagen–Poiseuille equation, and therefore this calculator, is appropriate.
| Aspect | Laminar flow (this calculator) | Turbulent flow |
|---|---|---|
| Typical Reynolds number | Re ≲ 2 000 | Re ≳ 4 000 (transitional in between) |
| Velocity profile | Smooth, parabolic profile; maximum at center, zero at wall | Flatter, more uniform profile with fluctuations and eddies |
| Pressure–flow relationship | Directly proportional (ΔP ∝ Q) | Nonlinear; depends on friction factor and roughness |
| Governing equation | Hagen–Poiseuille equation | Empirical correlations (e.g., Darcy–Weisbach with friction factor) |
| Typical applications | Microfluidics, narrow medical tubing, chromatography, small lab setups | Large water mains, industrial process lines, HVAC ducts |
| Suitability of this calculator | Appropriate, provided assumptions are met | Not appropriate; use turbulent flow methods instead |
The accuracy of the computed laminar flow rate depends on how closely your real system matches the assumptions built into the Hagen–Poiseuille equation. The main assumptions are:
If your system deviates from these conditions, the calculator may still provide a useful first estimate, but you should treat the result with caution and consider more detailed analysis or experimental measurement.
In particular, if the flow is likely turbulent (for example, high velocities in larger pipes or low-viscosity fluids like water or air at high flow rates), the predicted Q will underestimate the real pressure drop for a given flow or overestimate Q for a given pressure drop.
When using this calculator in design or analysis work, consider the following practical points:
For more advanced analysis, you may want to pair this calculator with tools for Reynolds number estimation, pressure drop in turbulent flow, or pump sizing so you can assess whether laminar assumptions remain valid across the entire operating range.
Use the Hagen–Poiseuille equation when flow is laminar, the pipe is straight and circular with constant radius, the fluid is Newtonian and incompressible, and entrance and exit effects are small relative to frictional losses along the pipe length.
The equation is written in terms of radius, but you can start from diameter D if you convert using r = D / 2. Be sure to convert units to meters and to apply the radius in the r4 term, not the diameter.
Under ideal laboratory conditions with well-characterized fluids and tubing, predictions can be quite accurate. In practical systems with fittings, bends, modest temperature variations, or uncertain viscosity data, results should be treated as approximate and validated experimentally when precision is critical.
Once flow transitions to turbulence, the relationship between pressure drop and flow rate changes, and the Hagen–Poiseuille equation no longer holds. In such cases, you must use turbulent flow correlations (for example, based on the Darcy–Weisbach equation and friction factors) rather than this laminar flow calculator.
Keep the pump gentle enough for laminar conditions while meeting each microfluidic demand spike. Your fingertips control the pressure drop—feel how and Reynolds number tug in opposite directions.
Drag or tap across the pipe to steer pressure; ← → keys provide fine nudges.
Sweet spot is active when the tube pulses aqua—hold there to chain combos.