Entrance-region heat transfer to blood steadily flowing in a pipe is studied. It is assumed that the non-Newtonian behaviour of blood can be expressed both by the Casson equation and the more complex law suggested by Merrill and Pelletier [J. Appl. Physiol.23, 179–182 (1967)]. The possible presence of a thin cell-free plasma layer at the wall is accounted for. The velocity distribution is determined analytically and a solution of the energy equation is obtained by a finite-difference method, for the two cases: (a) the uniform wall temperature, and (b) the uniform wall heat flux. Results are presented for the yield number Y ( = 2Rτy/σum) = 1, 5, 10 and 20 and the non-dimensional marginal layer thickness D ( = σ/R) = 0,0.0002, 0.01 and 0.1.
Laminar Heat Transfer Coefficients to Blood flowing in a Circular Duct / Dumas, Antonio; Barozzi, Giovanni Sebastiano. - In: INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER. - ISSN 0017-9310. - STAMPA. - 27:(1984), pp. 391-398. [10.1016/0017-9310(84)90286-2]
Laminar Heat Transfer Coefficients to Blood flowing in a Circular Duct
DUMAS, Antonio;BAROZZI, Giovanni Sebastiano
1984
Abstract
Entrance-region heat transfer to blood steadily flowing in a pipe is studied. It is assumed that the non-Newtonian behaviour of blood can be expressed both by the Casson equation and the more complex law suggested by Merrill and Pelletier [J. Appl. Physiol.23, 179–182 (1967)]. The possible presence of a thin cell-free plasma layer at the wall is accounted for. The velocity distribution is determined analytically and a solution of the energy equation is obtained by a finite-difference method, for the two cases: (a) the uniform wall temperature, and (b) the uniform wall heat flux. Results are presented for the yield number Y ( = 2Rτy/σum) = 1, 5, 10 and 20 and the non-dimensional marginal layer thickness D ( = σ/R) = 0,0.0002, 0.01 and 0.1.File | Dimensione | Formato | |
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