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A theoretic-experimental methodology is presented to d etermine the interstitial heat t ransfer coefficients in the water flow through packed b ed o f activated Bauxite, where the fluid is not i n h eat balance with the solid pha se. The heat transfer coefficients are obtained through "Single Blow Transient Method" combining the ex perimental results obtained in a test set-up with the numerical solutions of t he mathematical model. The system of partial differential equations generated in the mathematical model is solved through a numerical procedure based on the finite volumes method. Experimental test results and numerical solutions were obtained for different values of superficial speed of the fluid from the e ntrance of t he bed and for different porosity v alues, obtaining themselves that t he Nusselt numbers depend in great scale on the Reynolds numbers and the porosity of media.

CONVECCIÓN DE CALOR EN EL FLUJO DE FLUIDOS A TRAVÉS DE UN LECHO DE EMPAQUE DE BAUXITA ACTIVADA