Abstract
The aim of this work is to minimize the drying time of a polymer aqueous solution placed into a Petri dish while respecting strict constraints. Several experiments performed in a laboratory setup have shown the interest of a drying combining convective and infrared radiation as long as irradiation is correctly controlled. In this way, a one dimensional liquid diffusion model taking into account the product shrinkage was developed. Model predictions are in good adequacy to mass and temperature experimental data.
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Abbreviations
- a w :
-
water activity
- C p :
-
specific heat (J kg–1 K−1)
- D :
-
diffusion coefficient (m2 s−1)
- e :
-
thickness (m)
- E a :
-
activation energy (J mol−1)
- F m :
-
drying rate (kg m−2 s−1)
- h :
-
convective heat-transfer coefficient (W m−2 K−1)
- H air :
-
relative humidity (%)
- k m :
-
mass-transfer coefficient (m s−1)
- L v :
-
latent heat of vaporization (J kg−1)
- m :
-
mass of the product (kg)
- M v :
-
molecular weight (kg mol−1)
- P IR :
-
infrared irradiation (W m−2)
- P vsat :
-
saturated water vapor pressure (Pa)
- P va :
-
air vapor pressure (Pa)
- Q IR :
-
volume infrared power (W m−3)
- R :
-
gas constant (J K−1 mol−1)
- t :
-
time (s)
- T :
-
temperature (K)
- v :
-
velocity (m s−1)
- X :
-
moisture content (kg kg−1)
- z :
-
coordinate (m)
- ε :
-
emissivity
- ψ :
-
linear shrinkage coefficient
- κ :
-
extinction coefficient
- λ :
-
thermal conductivity (W m−1 K−1)
- ρ :
-
density (kg m−3)
- τ :
-
transmissivity
- σ :
-
Stefan–Boltzmann constant (W m−2 K−4)
- ξ :
-
dimensionless space coordinate
- + :
-
Petri dish
- d:
-
dried product
- m:
-
mean value
- p:
-
product
- w:
-
water
- i:
-
initial
- f:
-
final
- u:
-
upper
- l:
-
lower
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Allanic, N., Salagnac, P. & Glouannec, P. Convective and radiant drying of a polymer aqueous solution. Heat Mass Transfer 43, 1087–1095 (2007). https://doi.org/10.1007/s00231-006-0196-5
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DOI: https://doi.org/10.1007/s00231-006-0196-5