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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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 experimentPredict
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.
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Conditional fourth-power radius law
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) |
|---|---|
| 0.5 | 2.45437e-8 |
| 0.5375 | 3.27773e-8 |
| 0.575 | 4.29271e-8 |
| 0.6125 | 5.52693e-8 |
| 0.65 | 7.00992e-8 |
| 0.6875 | 8.77305e-8 |
| 0.725 | 1.08496e-7 |
| 0.7625 | 1.32745e-7 |
| 0.8 | 1.6085e-7 |
| 0.8375 | 1.93196e-7 |
| 0.875 | 2.30193e-7 |
| 0.9125 | 2.72265e-7 |
| 0.95 | 3.19856e-7 |
| 0.9875 | 3.73429e-7 |
| 1.025 | 4.33466e-7 |
| 1.0625 | 5.00467e-7 |
| 1.1 | 5.74951e-7 |
| 1.1375 | 6.57454e-7 |
| 1.175 | 7.48534e-7 |
| 1.2125 | 8.48764e-7 |
| 1.25 | 9.58738e-7 |
| 1.2875 | 0.00000107907 |
| 1.325 | 0.00000121038 |
| 1.3625 | 0.00000135334 |
| 1.4 | 0.00000150859 |
| 1.4375 | 0.00000167684 |
| 1.475 | 0.00000185878 |
| 1.5125 | 0.00000205514 |
| 1.55 | 0.00000226666 |
| 1.5875 | 0.00000249411 |
| 1.625 | 0.00000273825 |
| 1.6625 | 0.0000029999 |
| 1.7 | 0.00000327986 |
| 1.7375 | 0.00000357898 |
| 1.775 | 0.0000038981 |
| 1.8125 | 0.00000423811 |
| 1.85 | 0.00000459988 |
| 1.8875 | 0.00000498434 |
| 1.925 | 0.00000539241 |
| 1.9625 | 0.00000582504 |
| 2 | 0.00000628319 |
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.
| Quantity | Value | Unit |
|---|---|---|
| Conditional Poiseuille volume flow | 3.92699e-7 | m³/s |
| Conditional mean speed | 0.125 | m/s |
| Conditional Reynolds number | 250 | ratio |
| Regime code: 0 laminar screen, 1 transition, 2 turbulent screen | 0 | code |
| Conditional hydraulic loss power | 0.000392699 | W |
| Hydraulic resistance under laminar assumption | 2546480000 | Pa 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.
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Why can a larger-radius extrapolation fail even when the original narrow-tube measurement fit well?
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