Abstract
A model is proposed for the transfer of heat to non - Newtonian power - law fluids flowing in heated horizontal pipes. Comparisons with the existing models, based on the absolute-percent-arithmetic-average-deviation and the percent-standard-deviation, show that under the transitional and turbulent flow regimes the proposed correlation fits the experimental data more accurately over a wide range of flow behavior index and there are no restrictions for its use when applied to pseudoplastic fluids.
| Original language | American English |
|---|---|
| Journal | International Communications in Heat and Mass Transfer |
| Volume | 17 |
| DOIs | |
| State | Published - Mar 1 1990 |
Disciplines
- Complex Fluids
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