In supply chains of willow (Salix viminalis) biomass to energy plants, dryi
ng is advisable in order to enable safe long-term storage, increase boiler
efficiency and reduce gaseous emissions. To gain insight into the drying pr
ocess, drying characteristics of willow chips and stems were investigated e
xperimentally in a drying installation. The drying process was modelled wit
h a diffusion equation. The effective water diffusivity D-eff was assumed t
o be a simple algebraic function of the dimensionless moisture concentratio
n m: D-eff = D-0 m(a), with D-0 being the initial diffusivity, and a an emp
irical exponent. Drying of a chip and of a stem without bark could be succe
ssfully described with a diffusion equation for a plane sheet and a cylinde
r, respectively. Drying of a stem with bark could be successfully described
as drying of a stem without bark surrounded by a thin layer (bark) with a
much lower diffusivity. Compared to a chip, a stem without bark dried appro
ximately 10 times slower from fresh state to equilibrium moisture content,
mainly due to the larger diffusion distance of the stem. A stem with bark d
ried approximately 10 times slower than a stem without bark due to the low
diffusivity of the bark. (C) 2000 Silsoe Research Institute.