ISSN:
1431-4630
Keywords:
Key words Dehydration
;
Osmosis
;
Mathematical model
;
Mass transfer
;
[C Average sucrose concentration (g sucrose/g d.m.)
;
C* average dimensionless sucrose concentration
;
Cdis osmotic solution concentration (g sucrose/g d.m.)
;
Ce equilibrium sucrose concentration (g sucrose/g d.m.)
;
Co initial sucrose concentration (g sucrose/g d.m.)
;
Cl local sucrose concentration (g sucrose/g d.m.)
;
DSeff diffusivity coefficient of sucrose (m2/h)
;
DSo preexponential factor in Eq. 9
;
DWeff diffusivity coefficient of water (m2/h)
;
DWo preexponential factor in Eq. 8
;
ESa energy of activation in Eq. 9 (J/mol)
;
EWa energy of activation in Eq. 8 (J/mol)
;
L half-thickness of the solid (m)
;
Po initial sample weight (g)
;
Psso initial dry matter (g)
;
Pssf final dry matter (g)
;
Sy standard deviation (sample) (g water/g d.m.)2
;
Syx standard deviation (estimation) (g water/ g d.m.)2
;
%var percentage of explained variance
;
W average moisture content (g water/g d.m.)
;
We equilibrium moisture content (g water/g d.m.)
;
W1 local moisture content (g water/g d.m.)
;
Wo initial moisture content (g water/g d.m.)
;
WPsso moisture content referred to the initial dry matter (g water/ g d.m.)
;
x x-axis distance (m)
;
y y-axis distance (m)
;
z z-axis distance (m)
;
ΔW water losses (g)
;
ΔP mass losses (g)
;
ΔPss mass gain (g)
;
ΔPss/Psso solute gain referred to the initial dry matter (g solute/g d.m.)
;
Ψ dimensionless moisture content]
Source:
Springer Online Journal Archives 1860-2000
Topics:
Process Engineering, Biotechnology, Nutrition Technology
Notes:
Abstract The curves of dehydration by osmosis of 1 cm3 apple cubes have been simulated assuming the existence of two diffusional species. The diffusivity value of the two species, water and sucrose, was obtained by using a numerical method of non-linear regression analysis. The influence of the solution conditions (temperature and sucrose concentration) on the absorption rate was evaluated. Two sets of experiments were carried out: experiments at 70°Brix and different solution temperatures (30, 40, 50, 60 and 70 °C) on the one hand, and experiments at 50 °C and different solution concentrations (30, 50 and 70°Brix) on the other. The proposed diffusive model is able to explain 98% of the total variance. This model is also applicable to the simulation of dehydration by osmosis for other food products.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1007/s002170050065
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