Derive a pipe profile and then test its admissibility
For steady fully developed flow through a straight circular tube, an axial pressure drop supplies force on a cylindrical fluid core. Balancing it with shear around the core gives shear magnitude Δp r/(2L). Newtonian stress relates that shear to the radial velocity gradient.
Learning outcome: Derive the shear and velocity profiles, integrate their flow and independently check the regime before accepting any radius extrapolation.
Starting recap
Derive equations with their initial or boundary conditions, integrate distributed profiles, and check model domains independently of numerical outputs.
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At R = 0.001 m and Δp = 100 Pa, mean speed is 0.0125 m/s, center speed 0.025 m/s and Reynolds number 25. The wall shear magnitude is 0.05 Pa.
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At fixed fluid, pressure drop and length, doubling tube radius multiplies the conditional Reynolds number by:
Experiment
Derive the shear and velocity profiles, integrate their flow and independently check the regime before accepting any radius extrapolation.
Integrate a viscous profile and then audit its regime
Worked teaching model · synthetic values · Conditional steady fully developed laminar Newtonian flow in a straight circular1 m tube, viscosity.001 Pa s,density1000 kg/m³,no-slip wall. Report mathematical profile and Reynolds screen separately; Re2000 is a heuristic boundary, not observed turbulence. No clinical or apparatus application.
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Conditional parabolic profile, subject to regime screen
Unlike graph quantities rescale independently; read units and values, not screen angles. 1: DeltaP(R²−r²)/(4eta L) (solid). Joined curves show the supplied model, not additional observations.
Equivalent numerical coordinates for Conditional parabolic profile, subject to regime screen
DeltaP(R²−r²)/(4eta L)
| radial coordinate (m) | axial velocity (m/s) |
|---|---|
| -0.002 | 0 |
| -0.00195 | 0.009875 |
| -0.0019 | 0.0195 |
| -0.00185 | 0.028875 |
| -0.0018 | 0.038 |
| -0.00175 | 0.046875 |
| -0.0017 | 0.0555 |
| -0.00165 | 0.063875 |
| -0.0016 | 0.072 |
| -0.00155 | 0.079875 |
| -0.0015 | 0.0875 |
| -0.00145 | 0.094875 |
| -0.0014 | 0.102 |
| -0.00135 | 0.108875 |
| -0.0013 | 0.1155 |
| -0.00125 | 0.121875 |
| -0.0012 | 0.128 |
| -0.00115 | 0.133875 |
| -0.0011 | 0.1395 |
| -0.00105 | 0.144875 |
| -0.001 | 0.15 |
| -0.00095 | 0.154875 |
| -0.0009 | 0.1595 |
| -0.00085 | 0.163875 |
| -0.0008 | 0.168 |
| -0.00075 | 0.171875 |
| -0.0007 | 0.1755 |
| -0.00065 | 0.178875 |
| -0.0006 | 0.182 |
| -0.00055 | 0.184875 |
| -0.0005 | 0.1875 |
| -0.00045 | 0.189875 |
| -0.0004 | 0.192 |
| -0.00035 | 0.193875 |
| -0.0003 | 0.1955 |
| -0.00025 | 0.196875 |
| -0.0002 | 0.198 |
| -0.00015 | 0.198875 |
| -0.0001 | 0.1995 |
| -5.00000e-5 | 0.199875 |
| 0 | 0.2 |
| 5.00000e-5 | 0.199875 |
| 0.0001 | 0.1995 |
| 0.00015 | 0.198875 |
| 0.0002 | 0.198 |
| 0.00025 | 0.196875 |
| 0.0003 | 0.1955 |
| 0.00035 | 0.193875 |
| 0.0004 | 0.192 |
| 0.00045 | 0.189875 |
| 0.0005 | 0.1875 |
| 0.00055 | 0.184875 |
| 0.0006 | 0.182 |
| 0.00065 | 0.178875 |
| 0.0007 | 0.1755 |
| 0.00075 | 0.171875 |
| 0.0008 | 0.168 |
| 0.00085 | 0.163875 |
| 0.0009 | 0.1595 |
| 0.00095 | 0.154875 |
| 0.001 | 0.15 |
| 0.00105 | 0.144875 |
| 0.0011 | 0.1395 |
| 0.00115 | 0.133875 |
| 0.0012 | 0.128 |
| 0.00125 | 0.121875 |
| 0.0013 | 0.1155 |
| 0.00135 | 0.108875 |
| 0.0014 | 0.102 |
| 0.00145 | 0.094875 |
| 0.0015 | 0.0875 |
| 0.00155 | 0.079875 |
| 0.0016 | 0.072 |
| 0.00165 | 0.063875 |
| 0.0017 | 0.0555 |
| 0.00175 | 0.046875 |
| 0.0018 | 0.038 |
| 0.00185 | 0.028875 |
| 0.0019 | 0.0195 |
| 0.00195 | 0.009875 |
| 0.002 | 0 |
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 mean speed | 0.1 | m/s |
| Conditional maximum speed | 0.2 | m/s |
| Conditional volume flow | 1.25664e-6 | m³/s |
| Conditional Reynolds number | 400 | ratio |
| Laminar heuristic screen below2000 | 1 | flag |
| Wall shear-stress magnitude | 0.2 | Pa |
The supplied laminar profile passes the stated Reynolds screen, not an empirical regime certification.
Axial force balance on a cylindrical core gives shear magnitude DeltaP r/(2L). Newtonian stress with no-slip wall integrates to v(r)=DeltaP(R²−r²)/(4eta L). Integrate2pi r v dr for Q=pi DeltaP R⁴/(8eta L), yielding vmax=2vmean. At fixed pressure drop, Reynolds scales R³, so radius extrapolation can invalidate the starting model.
Predict before inspecting the values. Save contrasting records with assumptions and one alternative explanation. This virtual display does not certify practical measurement technique.
The supplied laminar profile passes the stated Reynolds screen, not an empirical regime certification.
Axial force balance on a cylindrical core gives shear magnitude DeltaP r/(2L). Newtonian stress with no-slip wall integrates to v(r)=DeltaP(R²−r²)/(4eta L). Integrate2pi r v dr for Q=pi DeltaP R⁴/(8eta L), yielding vmax=2vmean. At fixed pressure drop, Reynolds scales R³, so radius extrapolation can invalidate the starting model.
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