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An irreversible thermodynamics model for unsteady-state nonisothermal moisture diffusion in wood
Authors:Dr S Avramidis  Dr S G Hatzikiriakos  Dr J F Siau
Institution:(1) Department of Wood Science, University of British Columbia, V6T 1Z4 Vancouver, B.C., Canada;(2) Department of Chemical Engineering, University of British Columbia, V6T 1Z4 Vancouver, B.C., Canada;(3) P.O. Box 41, 12942 Keene, NY, USA
Abstract:Summary A model that predicts heat and moisture transfer through wood in the hygroscopic range and which is based on the principles of irreversible thermodynamics, was evaluated with unsteady-state nonisothermal moisture desorption experimental data. The model predicted the phenomenon of thermal diffusion during the initial stages of desorption and results in a very good simulation of the desorption curve and the center's temperature change with time.Symbols Cp specific heat of air (= 0.24 cal/g K @ 70 °C) - CT specific heat of wood, cal/g K - D transverse diffusion coefficient, cm2/s - Eb activation energy, cal/mol - Eo heat of vaporization, cal/mol - EL differential heat of sorption, cal/mol - G specific gravity of wood - H relative humidity, % - hT convective heat transfer coefficient, cal/cm2 s K - hc convective mass transfer coefficient based on the concentration of moisture in wood, cm/s - hv convective mass transfer coefficient based on the concentration of moisture in the air in equilibrium with the wood surface, cm/s - KM coefficient for diffusion due to moisture gradient, g/cm s % - KT transverse thermal conductivity coefficient, cal/cm K s - M moisture content, % - Po saturated vapor pressure, atm - R universal gas constant, cal/mol K (= 82.056 cm3 atm/mol K) - t time, s - T temperature, K - x distance, cm Greek Letters epsi evaporation or condensation criterion - rgr wood density, g/cm3 - rgrW water density (=1), g/cm3 - rgra air density, g/cm3 Department of Wood Science and Forest Products Virginia Polytechnic Institute and State University Blackburg, Virginia 24061-0503
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