Simulation of heat transfer to a canned corn starch dispersion subjected to axial rotation

Author(s):  
J. Tattiyakul ◽  
M.A. Rao ◽  
A.K. Datta
2002 ◽  
Vol 54 (4) ◽  
pp. 321-329 ◽  
Author(s):  
J. Tattiyakul ◽  
M.A. Rao ◽  
A.K. Datta

Author(s):  
Hussein F. Hassan ◽  
Hosahalli S. Ramaswamy ◽  
Mritunjay Dwivedi

Abstract Heat transfer to canned particulates in non-Newtonian fluids (Nylon particles suspended in aqueous carboxymethyl cellulose - CMC - solution) during fixed and free bi-axial rotation was studied in a pilot-scale, full water-immersion single-cage rotary retort. A response surface methodology was used in order to study the effect of different process parameters, including rotational speed (7-23 rpm), CMC concentration (0.0-1.0%) and retort temperature (110-130C), at five levels of each, on overall heat transfer coefficient (U) and fluid to particle heat transfer coefficient (hfp) in both rotation modes. The analysis of variance showed that the rotational speed, CMC concentration and retort temperature were significant (p < 0.05) factors for hfp in the following order: rotation speed > CMC concentration > retort temperature; however, only rotational speed and CMC concentration were significant (p < 0.05) factors for U. With an increase in rotational speed and retort temperature, there was an increase in the associated U and hfp values; however, increasing the CMC concentration resulted in the opposite. Using the numerical optimization of the Design Expert software, optimum heat transfer was found at a rotational speed of 20 rpm, CMC concentration of 0.6% and retort temperature of 126C. T-test revealed that both U and hfp were significantly (p < 0.05) higher in the free bi-axial mode as compared to the fixed axial mode of rotation.


1992 ◽  
Vol 114 (2) ◽  
pp. 418-424 ◽  
Author(s):  
C. J. Ho ◽  
F. J. Tu

A numerical investigation is made to evaluate the perturbing effect of forced convection due to axial rotation of the inner cylinder on natural convection heat transfer of cold water with density inversion effects in a vertical cylindrical annulus. The mixed convection heat and fluid flow structures in the annulus are found to be strongly affected by the density inversion effects. The centrifugally forced convection can result in significant enhancement of the buoyant convection heat transfer of cold water with the density inversion parameter being equal to 0.4 or 0.5; thus the slow axial rotation of the inner cylinder can be a viable means for heat transfer augmentation of cold water natural convection in a vertical annulus.


1995 ◽  
Vol 2 (2) ◽  
pp. 123-129 ◽  
Author(s):  
Shuichi Torii ◽  
Wen-Jei Yang

A numerical study is performed to investigate turbulent flow and heat transfer characteristics in the entrance region of a pipe rotating around its axis. Various different k-ε turbulence models are employed whose function consists of the Richardson number in the e model to take swirling into account. The axial rotation of the pipe suppresses thermal development and causes a substantial decrease in the Nusselt number along the flow. It is disclosed from the study that an increase in the rotation rate induces a reduction in the velocity gradient, turbulent kinetic energy and Reynolds stress in the vicinity of the wall and a substantial deformation of these radial profiles in the downstream direction. It results in both a suppression of the thermal development and an attenuation in the Nusselt number along the flow.


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