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Measurement of Heat Transfer Coefficients Using Stationary and Moving Particles in Tube Flow
The design of thermal processes for particulate foods depends strongly on values of fluid-to-particle heat transfer coefficient ( h fp ) as well as on the heat penetration and particulate flow data during continuous processes. The stationary and moving thermocouple experimental techniques were used...
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Published in: | Food and bioproducts processing 1999-09, Vol.77 (3), p.213-222 |
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Main Authors: | , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | The design of thermal processes for particulate foods depends strongly on values of fluid-to-particle heat transfer coefficient (
h
fp
) as well as on the heat penetration and particulate flow data during continuous processes. The stationary and moving thermocouple experimental techniques were used to simulate the heat transfer between a fluid and a particle in tube flow using water and carboxymethylcellulose (CMC) solutions. The fluid viscosity was found to significantly affect
h
fp
; an increase in the fluid viscosity decreased the value of
h
fp
. An increase in the particle size within the tube flow increased
h
fp
while particle shape had little effect on
h
fp
. A dimensionless Nusselt correlation was also obtained in terms of the generalized Reynolds and Prandtl numbers for both the Newtonian and non-Newtonian fluids. The correlation showed strong agreement with experimental values and other models published in literature. |
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ISSN: | 0960-3085 1744-3571 |
DOI: | 10.1205/096030899532493 |