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For steady laminar Newtonian flow in a long straight circular tube, Poiseuille relates volume flow to pressure drop and viscosity.
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Formula
Q in m3/s; r and L in m; Δp in Pa; η in Pa·s
| Symbol | Meaning | Unit |
|---|---|---|
| Volume flow through the tube | m3/s | |
| Inside tube radius | m | |
| Pressure drop along the tube | Pa | |
| Dynamic viscosity | Pa·s | |
| Tube length | m |
Q=\frac{\pi r^4\Delta p}{8\eta L}The solution assumes steady, fully developed laminar flow of an incompressible Newtonian liquid through a straight circular tube with no-slip at the wall. Radius enters to the fourth power: halving it reduces flow to one-sixteenth at otherwise fixed conditions. The simple relation does not apply to turbulent flow, noncircular ducts or entrance regions.
The solution assumes steady, fully developed laminar flow of an incompressible Newtonian liquid through a straight circular tube with no-slip at the wall. Radius enters to the fourth power: halving it reduces flow to one-sixteenth at otherwise fixed conditions. The simple relation does not apply to turbulent flow, noncircular ducts or entrance regions.
For steady laminar Newtonian flow in a long straight circular tube, Poiseuille relates volume flow to pressure drop and viscosity.
Base equation for the target quantity
Preserve signs, boundary conditions and units when rearranging.
Work through the numerical example for “Hagen–Poiseuille law for laminar pipe flow” and check its unit and magnitude.
For water with η=1.0 mPa·s, r=1 mm, L=0.20 m and Δp=100 Pa, Q≈1.96×10−7 m3/s.
Substituting a related quantity that shares the same symbol.
Use variable definitions and check: Q in m3/s; r and L in m; Δp in Pa; η in Pa·s.
Formula cluster
For steady laminar Newtonian flow in a long straight circular tube, Poiseuille relates volume flow to pressure drop and viscosity.
For water with η=1.0 mPa·s, r=1 mm, L=0.20 m and Δp=100 Pa, Q≈1.96×10−7 m3/s.
Analyze laminar pressure-driven flow in capillaries and narrow tubes.
Here is how to work through a typical Hagen–Poiseuille law for laminar pipe flow (Q = πr⁴Δp/(8ηL)) task step by step:
Task
Work through the numerical example for “Hagen–Poiseuille law for laminar pipe flow” and check its unit and magnitude.
Solution path
For water with η=1.0 mPa·s, r=1 mm, L=0.20 m and Δp=100 Pa, Q≈1.96×10−7 m3/s.
The parabolic laminar pipe velocity profile is set by shear and the no-slip boundary condition. Integrating that profile over the circular area produces the fourth power of radius. Halving radius cuts flow to one-sixteenth if pressure gradient and other quantities stay fixed. Poiseuille flow assumes a Newtonian incompressible fluid, steady fully developed laminar motion and a long straight circular tube with no slip. Radius enters to the fourth power, so small radius errors matter greatly. The relation does not apply to turbulent or entrance-region flow.
First compute Reynolds number using pipe diameter as characteristic length and appropriate fluid properties. Poiseuille requires laminar, fully developed pipe flow; one transition threshold is not universal because of inlet, roughness and disturbances. Check geometry and boundary conditions too. Poiseuille flow assumes a Newtonian incompressible fluid, steady fully developed laminar motion and a long straight circular tube with no slip. Radius enters to the fourth power, so small radius errors matter greatly. The relation does not apply to turbulent or entrance-region flow.
In the equation, Q is proportional to Δp when Δp means inlet pressure minus outlet pressure. Positive flow then goes from higher to lower pressure. Reverse the pressure-difference definition and Q changes sign. Define orientation before calculating. Poiseuille flow assumes a Newtonian incompressible fluid, steady fully developed laminar motion and a long straight circular tube with no slip. Radius enters to the fourth power, so small radius errors matter greatly. The relation does not apply to turbulent or entrance-region flow.
Write the quantity and unit from the variable list next to every value: Q in m3/s; r and L in m; Δp in Pa; η in Pa·s. Substitute only after converting to a consistent unit system, and state sign or reference direction explicitly. The example For water with η=1.0 mPa·s, r=1 mm, L=0.20 m and Δp=100 Pa, Q≈1.96×10−7 m3/s. is a calculation check: result, unit and order of magnitude must fit the described situation. Round after intermediate calculations so small contributions are not lost prematurely. Poiseuille flow assumes a Newtonian incompressible fluid, steady fully developed laminar motion and a long straight circular tube with no slip. Radius enters to the fourth power, so small radius errors matter greatly. The relation does not apply to turbulent or entrance-region flow.
The background states this starting condition: The solution assumes steady, fully developed laminar flow of an incompressible Newtonian liquid through a straight circular tube. That limits when the result is a valid model prediction. Compare the problem’s boundary conditions with this assumption before substituting values; real components, material properties or loads can introduce additional effects. The cited reference supports the relation used here but does not remove the need to check whether the specific case fits the model. Poiseuille flow assumes a Newtonian incompressible fluid, steady fully developed laminar motion and a long straight circular tube with no slip. Radius enters to the fourth power, so small radius errors matter greatly. The relation does not apply to turbulent or entrance-region flow.
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Which formula describes Hagen–Poiseuille law for laminar pipe flow?
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Which common mistake happens with Hagen–Poiseuille law for laminar pipe flow?
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