Heat and mass transfer studies were conducted with pasta cylinders at
different porosities, temperatures and pressures. Tests with pasta cyl
inders were conducted at porosities of 6 and 26%, temperatures of 40,
55, 71 and 105 degrees C and total pressures of 77, 101 and 202 kPa. A
nalysis of tests conducted with 3.18, 4.76 and 5.56 mm diameter dense
pasta cylinders (6% porosity) at 71 degrees C indicated that mass tran
sfer was consistent with control by internal diffusion. The drying not
affected by total pressure, suggesting that the mechanism of internal
moisture movement is best considered a liquid or adsorbed phase diffu
sion phenomenon. Effective moisture diffusivities of dense pasta incre
ased as temperature and moisture content increased, with values rangin
g from 8 to 106 x 10(-12) m(2)/s. Diffusivities of porous pasta (26% p
orosity) ranged from 36 to 221 x 10(-12) m(2)/s. Heat transfer studies
with dense and porous pasta indicated that the center temperature for
5.56 mm diameter pasta cylinders approached the dry bulb air temperat
ure within 3 degrees C in less than 10 min, supporting the assumption
that pasta drying can be considered an isothermal process. A semi-empi
rical model for moisture diffusivity in pasta that accounts for the ef
fects of porosity, pressure and moisture binding was developed. The mo
del agrees reasonable well with experimental data for dense pasta, and
for porous pasta aat low and atmospheric pressures (77 kPa and 101 kP
a). The model underpredicts the moisture diffusivity for porous pasta
at high pressures (202 kPa). The model provides a reasonable estimate
of moisture diffusivity in pasta. (C) 1996 Elsevier Science Limited.