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SCIENCE · INVESTIGATE AND EXPLAIN

Check whether a fourth-power flow prediction remains admissible

Viscosity describes resistance to relative motion between neighboring fluid layers. A Newtonian fluid has shear stress proportional to velocity gradient, with viscosity η in Pa s. Laminar flow has organized layers; turbulent flow includes irregular fluctuations and mixing. A smooth tube does not guarantee laminar flow at every speed.

Learning outcome: Predict the radius ratios for flow, speed and Reynolds number before changing radius. Retain at least one screened laminar and one rejected case, and explain which independent premises a Reynolds screen cannot establish.

Starting recap

Declare density, pressure reference, flow regime and admissible force constraints. Convert area and volume units before balancing forces, mass or energy.

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Try

At radius 2 mm and pressure drop 1600 Pa, conditional speed is 0.8 m/s and Reynolds number 3200. The laminar relation fails its own screening premise; do not report its conditional flow as a verified actual value.

Open the experiment

Predict

Doubling radius at fixed Δp, η and L multiplies conditional Poiseuille flow by:

Experiment

Predict the radius ratios for flow, speed and Reynolds number before changing radius. Retain at least one screened laminar and one rejected case, and explain which independent premises a Reynolds screen cannot establish.

Screen a Poiseuille prediction against its own regime

Worked teaching model · synthetic values · Hypothetical Newtonian liquid rho=1000 kg/m³, viscosity .001 Pa s, length 1 m. Straight uniform round tube, no-slip wall, fully developed laminar relation used conditionally. Reynolds thresholds 2000 and 3000 are approximate screening guides, not universal guarantees.

Reset keeps your prediction, captures and practice history.

Conditional fourth-power radius law

conditional flow (m³/s)radius (mm)020.000006283190

Unlike graph quantities rescale independently; read units and values, not screen angles. 1: requires laminar premises (solid). Joined curves show the supplied model, not additional observations.

Equivalent numerical coordinates for Conditional fourth-power radius law

requires laminar premises

radius (mm)conditional flow (m³/s)
0.52.45437e-8
0.53753.27773e-8
0.5754.29271e-8
0.61255.52693e-8
0.657.00992e-8
0.68758.77305e-8
0.7251.08496e-7
0.76251.32745e-7
0.81.6085e-7
0.83751.93196e-7
0.8752.30193e-7
0.91252.72265e-7
0.953.19856e-7
0.98753.73429e-7
1.0254.33466e-7
1.06255.00467e-7
1.15.74951e-7
1.13756.57454e-7
1.1757.48534e-7
1.21258.48764e-7
1.259.58738e-7
1.28750.00000107907
1.3250.00000121038
1.36250.00000135334
1.40.00000150859
1.43750.00000167684
1.4750.00000185878
1.51250.00000205514
1.550.00000226666
1.58750.00000249411
1.6250.00000273825
1.66250.0000029999
1.70.00000327986
1.73750.00000357898
1.7750.0000038981
1.81250.00000423811
1.850.00000459988
1.88750.00000498434
1.9250.00000539241
1.96250.00000582504
20.00000628319

At most 82 representative computed coordinates including endpoints; the plotted curve can use a finer grid. A table of a revealed generator is not independent measurement evidence.

Calculated quantities under the declared measurement model
QuantityValueUnit
Conditional Poiseuille volume flow3.92699e-7m³/s
Conditional mean speed0.125m/s
Conditional Reynolds number250ratio
Regime code: 0 laminar screen, 1 transition, 2 turbulent screen0code
Conditional hydraulic loss power0.000392699W
Hydraulic resistance under laminar assumption2546480000Pa s/m³

The conditional solution passes the approximate laminar screen, subject to the other stated premises.

For fully developed laminar Newtonian tube flow, Q=pi r⁴ Delta p/(8 eta L). Reynolds number uses mean speed and diameter. Doubling radius at fixed pressure drop multiplies conditional Q by 16, speed by 4 and Reynolds number by 8; the changed state may invalidate the original law. Entrance effects, roughness and unsteadiness are outside this bounded packet.

Predict before inspecting the values. Save contrasting records with assumptions and one alternative explanation. This virtual display does not certify practical measurement technique.

The conditional solution passes the approximate laminar screen, subject to the other stated premises.

For fully developed laminar Newtonian tube flow, Q=pi r⁴ Delta p/(8 eta L). Reynolds number uses mean speed and diameter. Doubling radius at fixed pressure drop multiplies conditional Q by 16, speed by 4 and Reynolds number by 8; the changed state may invalidate the original law. Entrance effects, roughness and unsteadiness are outside this bounded packet.

Captures preserve recipes and replay their calculated results. They are synthetic model evidence, not physical measurements.

Understand

Declare the fluid, reference and evidence

Viscosity describes resistance to relative motion between neighboring fluid layers. A Newtonian fluid has shear stress proportional to velocity gradient, with viscosity η in Pa s. Laminar flow has organized layers; turbulent flow includes irregular fluctuations and mixing. A smooth tube does not guarantee laminar flow at every speed.

Build the algebraic model

For fully developed laminar flow in a straight round tube with no slip at the wall, Poiseuille’s relation is Q=πr⁴Δp/(8ηL). It assumes a Newtonian incompressible fluid and a pressure drop allocated to that developed section. At fixed pressure drop, doubling radius would multiply conditional flow by 16 and mean speed by four. This strong geometric effect does not excuse checking the assumptions again.

Check the original numerical packet

The workbench uses density 1000 kg/m³, viscosity 0.001 Pa s and length 1 m. At radius 1 mm and pressure drop 1000 Pa, conditional Q=3.92699×10⁻⁷ m³/s, mean speed 0.125 m/s and Reynolds number 2ρvr/η=250. Doubling radius gives conditional Reynolds number 2000, at the approximate transition boundary, not a secure new laminar prediction. The plotted curve remains explicitly conditional outside the screened branch.

Challenge the assumptions and transfer

Reynolds thresholds near 2000 and 3000 are approximate tube-flow guides; entrance geometry, roughness and disturbances matter. In a separate low-Reynolds sphere model, supplied Stokes drag is 6πηrv, so doubling speed doubles drag; a quadratic high-speed model instead quadruples it. Molecular diffusion is transport down a concentration gradient without requiring bulk flow: under a supplied one-dimensional relation rms distance=√(2Dt), quadrupling time doubles distance. Osmosis concerns solvent transport across a selectively permeable boundary, not unrestricted solute diffusion. For a supplied dilute ideal osmotic law Δπ=RTΔc, doubling concentration difference at fixed temperature doubles pressure difference. These are model-comparison actions, not medical guidance or exposure experiments.

Worked original case

At radius 2 mm and pressure drop 1600 Pa, conditional speed is 0.8 m/s and Reynolds number 3200. The laminar relation fails its own screening premise; do not report its conditional flow as a verified actual value.

Bounded investigation

Predict the radius ratios for flow, speed and Reynolds number before changing radius. Retain at least one screened laminar and one rejected case, and explain which independent premises a Reynolds screen cannot establish.

Changed-case numerical practice

Try the changed case before feedback

A conditional laminar tube flow has Reynolds number 150 at radius r. At the same pressure drop, viscosity, density and length, what is the conditional Reynolds number at 2r?

This practice is public and unsaved. A matching number does not verify understanding. Retain your explanation, assumptions and changed-case evidence in the separate course workspace.

Sources and limits

Original content checked 30 October 2026 against OpenStax College Physics 2e. All records are supplied or generated educational evidence. No pressure rigs, liquid handling, bodily measurements or physical exposure protocols are requested. Virtual admissibility does not certify real equipment safety, practical skill or independent mastery.

Apply

Doubling radius at fixed Δp, η and L multiplies conditional Poiseuille flow by:

Public practice checks a specific claim. It does not establish independent mastery.

Why can a larger-radius extrapolation fail even when the original narrow-tube measurement fit well?

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