A deterministic model was developed to perform a board-by-board simula
tion of a forced convective batch lumber kiln. Individual board proper
ties may be input and dryer operating parameters varied. The drying ra
tes are empirical correlations based on single-board laboratory tests.
The model incorporates the thermodynamic properties of the wood and g
as, as well as mass and energy balances within the lumber stack. It al
so accounts for differences in heat and mass transfer resulting from p
osition and changing gas properties throughout the dryer. The rate of
drying predicted by the model and the final moisture content distribut
ion were verified by weighing boards in a batch kiln before, during, a
nd after drying. The application of the model is illustrated by simula
ting four common scenarios.