A steady state mathematical model which describes a natural gas indire
ct fired baking tunnel-oven is presented. Heat and mass transfer were
studied. Individual heat transfer modes taken into account were radiat
ion, convection and conduction. It was assumed that the baking chamber
was homogeneous between roof and base. A homogeneous moisture and tem
perature distribution was assumed for the biscuit. The flow of air ins
ide the oven and the drying of the biscuit were studied. A water activ
ity model at high temperature was used. The model simulations provide
spatial distributions of temperature and moisture of the biscuit, and
temperature and hygrometry of the air. Experiments were performed at d
ifferent baking conditions. Data were compared with numerical results.
Good agreement was obtained between the experimental results and the
model predictions.