A theoretical treatment IS presented which allows radml temperature and velocity profiles and the axial pressure profile to be pre&cted when VLSCOUS Newtoman and non-Newtonian flmds are heated or cooled m lammar flow m cucular tubes The overall heat transfer rate can also be pre&cted m the form of a
Heat transfer to Newtonian and non-Newtonian fluids flowing in a laminar regime
โ Scribed by J.C. Gottifredi; O.D. Quiroga; A.F. Flores
- Publisher
- Elsevier Science
- Year
- 1983
- Tongue
- English
- Weight
- 461 KB
- Volume
- 26
- Category
- Article
- ISSN
- 0017-9310
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โฆ Synopsis
A new analytical approach is presented to estimate the local and mean heat flux from a wall maintainedat a given temperatureto a fluid flowing in a laminarregime. Theprocedurecan beapplied to the analysis of planeas well as cylindrical geometry configurations while the fluid behaviourcan be considered Newtonian or non-Newtonian providedthe axialvelocity distributioncan be represented by an analytical function of position. The method is simple and gives veryaccurateresults when comparedwithnumerical estimates previously presented in the literature. Anumberofcomparisons arepresented in thisworkshowing that maximum deviations are always below 3.5%in terms of mixing cup temperature. The technique is so simplethat it should be useful for the analysis ofsimilarproblems in the field of convective heat and mass transfer.
l'\O~IEl'\CLATURE Ai()
๐ SIMILAR VOLUMES
The main objective of this work is the consideration of local heat transfer coefficients for non-Newtonian power-law pseudoplastic liquid in laminar flow in circular conduits. The wall boundary conditions chosen are cases involving uniformly constant heat flux and step change in heat flux. Analytica