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Biosystems Engineering
Volume 90, Issue 3, March 2005, Pages 289-294
 
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doi:10.1016/j.biosystemseng.2004.10.009    
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Copyright © 2004 Silsoe Research Institute Published by Elsevier Ltd.

Modelling of Solute Aqueous Extraction from Carrots subjected to a Pulsed Electric Field Pre-treatment

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K. El-belghiti and E. VorobievCorresponding Author Contact Information, E-mail The Corresponding Author

Equipe Technologies Agro-Industrielles, UMR 6067 Unité Génie des Procédés Industriels, Département Génie Chimique, Université de Technologie de Compiègne, Centre de Recherche de Royallieu, BP 20529-60205 Compiègne Cedex, France


Received 29 March 2004; 
accepted 22 October 2004. 
Available online 4 February 2005.

This study is devoted to solid–liquid extraction from carrot samples subjected to pulsed electric fields (PEF) of different energy levels. Aqueous extraction of solute from carrot samples prepared in the forms of disc or slices (coarse and fine) was conducted at room temperature with and without agitation. A two-exponential kinetic model corresponding to the two-stage extraction (rapid washing and slow diffusion) described successfully the experimental data. For the studied carrot samples, the solute yield increased with the increase in energy level up to a threshold value of 9 kJ/kg. Furthermore, the increase in stirring speed up to 250 min−1 enhanced extraction kinetics. Finally, fragmentation of carrot particles increased the solute yield obtained during the washing stage of extraction.

Notation

c
solute concentration in the solution at any time during the extraction process, g [solubles]/100 g [juice]
c0
solute concentration of fresh sugar beet juice (initial solute concentration), g [solubles]/100 g [juice]
c*
dimensionless solute concentration in the solution at any time during the extraction process
cd
equilibrium solute concentration in the solution due to the diffusion process, g [solubles]/100 g [juice]
View the MathML source
dimensionless equilibrium solute concentration in the solution due to the diffusion process
cw
equilibrium solute concentration in the solution due to the washing process, g [solubles]/100 g [juice]
View the MathML source
dimensionless equilibrium solute concentration in the solution due to the washing process
c
total equilibrium solute concentration, g [solubles]/100 g [juice]
d
distance between electrodes, mm
E
intensity of pulsed electric field, V/cm
I
amplitude of electric current strength, A
kd
rate constant for the diffusion process, min−1
kw
rate constant for the washing process, min−1
L
extract volume, m3
m
mass of sample, kg
N
number of pulses
n
liquid to solid ratio
S
solid volume, m3
t
time, min
tPEF
PEF treatment duration, s
U
current tension, V
W
specific energy consumption during the PEF treatment, kJ/kg
τ
duration of pulse, s

Article Outline

Nomenclature
1. Introduction
2. Materials and methods
3. Results and discussion
3.1. Reproducibility of results
3.2. Effect of pulsed electric field parameters
3.3. Effect of stirring
3.4. Effect of sample type
4. Conclusion
References








Corresponding Author Contact InformationCorresponding author.

Biosystems Engineering
Volume 90, Issue 3, March 2005, Pages 289-294
 
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