Heat Transfer in Food Products

Keyword(s):  
1988 ◽  
Vol 8 (2) ◽  
pp. 141-142
Author(s):  
Dean Burfoot ◽  
Colin Bailey
Keyword(s):  

1976 ◽  
Vol 19 (3) ◽  
pp. 0577-0583 ◽  
Author(s):  
S. Srinivasa Murthy ◽  
M. V. Krishna Murthy ◽  
A. Ramachandran
Keyword(s):  

1974 ◽  
Vol 17 (4) ◽  
pp. 0769-0773 ◽  
Author(s):  
S. Srinivasa Murthy ◽  
M. V. Krishna Murthy ◽  
A. Ramachandran

2008 ◽  
Vol 99 (2) ◽  
pp. 228-233 ◽  
Author(s):  
Ravi Kumar ◽  
Anil Kumar ◽  
U. Narayana Murthy

2015 ◽  
Vol 149 ◽  
pp. 78-86 ◽  
Author(s):  
O. Laguerre ◽  
S. Duret ◽  
H.M. Hoang ◽  
L. Guillier ◽  
D. Flick

1989 ◽  
Vol 7 (3) ◽  
pp. 621-624
Author(s):  
T. Kudra ◽  
G.S.V. Raghavan
Keyword(s):  

1980 ◽  
Vol 102 (4) ◽  
pp. 761-765 ◽  
Author(s):  
P. M. Abdul Majeed

Hydrair cooling of perishable food products is expected to incorporate the advantages of both air cooling and hydrocooling processes. This technique consists of passing cold air over a product which is continuously wetted by a spray of chilled water. In this paper, a mathematical model for the hydrair cooling of slab-shaped food products is proposed. The set of differential equations for heat transfer through the product and the wetting liquid are solved simultaneously, using finite difference method. It is observed that the process of hydrair cooling is advantageous at lower values of the film Reynolds number for higher Biot number values. The cooling speed and the governing parameters are correlated.


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