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CHE-40

Dittus–Boelter Nu

Turbulent pipe Nusselt.

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GoverningDittus–Boelter Nu

Governing equation

Nu=0.023Re0.8PrnNu=0.023 Re^{0.8} Pr^{n}

where

Re
Re ()
Pr
Pr ()
n
n ()
Nu
Dittus–Boelter Nu ()

Lecture brief

Historical brief

From CSTR/PFR mole balances and Arrhenius rates to McCabe–Thiele stages and NTU exchangers, chemical engineering is conservation plus equilibrium. The lab is that design arithmetic. This sheet (CHE-40 — Dittus–Boelter Nu) is the form associated with Dittus–Boelter Nu. Working symbols: ReRe, PrPr, nn \rightarrow NuNu. Turbulent pipe Nusselt. Pedagogical SI sheet with a live model and a swept parameter.

Purpose

Purpose: compute NuNu from ReRe, PrPr, nn in Chemical engineering via Nu=0.023Re0.8PrnNu=0.023 Re^{0.8} Pr^{n} Turbulent pipe Nusselt. Use it when a real chemical engineering question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given Re=20000.000Re = 20000.000\,\mathrm{—}, Pr=7.000Pr = 7.000\,\mathrm{—}, n=0.400n = 0.400\,\mathrm{—}, the governing relation Nu=0.023Re0.8PrnNu=0.023 Re^{0.8} Pr^{n} yields Nu=138.226Nu = 138.226\,\mathrm{—}. One governing identity, SI units, a single sweep on the sheet. Move a slider: the numbers are this situation, not a canned story.

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Inputs

Outputs

  • Dittus–Boelter Nu Nu138.226
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Narration of this film

One governing identity, SI units, a single sweep on the sheet.

Turbulent pipe Nusselt. Pedagogical SI sheet with a live model and a swept parameter.

Reading speed

Watch on YouTube