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Comparison of Drying and Quality Characteristics of Pear (Pyrus Communis L.) Using Mid-Infrared-Freeze Drying and Single Stage of Freeze Drying

  • Tamás Antal EMAIL logo , Judit Tarek-Tilistyák , Zoltán Cziáky and László Sinka
Published/Copyright: February 9, 2017

Abstract

This article provides results of an experimental investigation of hybrid- (MIR-FD), mid-infrared- (MIR) and freeze drying (FD) on the drying characteristics, energy consumption and quality parameters of pear. Rehydration ratio, color, texture, water activity, phenolic content and antioxidant activity were measured to evaluate the quality of dried pear products. Mid-infrared-freeze drying (MIR-FD) had the higher drying rate, which reduced the drying time by 14.3–42.9 % compared with FD method. Two empirical models were chosen to fit the drying curves and the models had the suitable R2 and RMSE values. Temperature characteristics of MIR and MIR-FD dried pear were determined in terms of interior temperature variation. The MIR-FD pear had darker color, better rehydration capacity, similar water activity, lower hardness (except of MIR-FD70°C) and highest content of chemical composition than single stage of FD products. Above all, the MIR50-60°C-FD was suggested as the best drying method for pear in this study.

Nomenclature

Superscripts

a*color parameter, dimensionless [degree of redness (+) and greenness (-)]
a, b, c, ddrying coefficients, dimensionless
aveaverage data
b*color parameter, dimensionless [degree of yellowness (+) and blueness (-)]
CChroma, dimensionless
DRdrying rate, kg·kg−1·min−1
ΔEtotal color difference, dimensionless
Δttime difference, h, min
Eelectrical power consumption, kJ
expexperimental data
hhue angle, °
kdrying constant, dimensionless
L*color parameter, dimensionless [degree of lightness (100) and darkness (0)]
Meequilibrium moisture content, kg H2O kg dm−1
mfdry matter weight of the material, kg
M0initial moisture content, kg H2O kg dm−1
MRmoisture ratio, dimensionless
Mtmoisture content at time t on dry basis, kg H2O kg dm−1
mtweight of material at specific time, kg
Nnumber of observations
prepredicted data
RMSEroot mean square error
R2coefficient of determination
RRrehydration ratio, dimensionless
SECspecific energy consumption, MJ kg H2O−1
tdrying time, h, min
W0initial mass of the raw material, kg
Wdweight of the dry sample used for rehydration, g
Wffinal mass of the dried sample, kg
Wrdrained weight of the rehydrated sample, g

Symbols

awwater activity, dimensionless
d.b.dry basis
Fforce, N
FDfreeze drying
IR intensitykW m−2
MIRmid-infrared drying
MIR-FDmid-infrared assisted freeze drying
p < 0.05significant difference
Tdrying and product temperature, °C
TAAtotal antioxidant capacity, µg GAE 100 g−1
TPstotal phenolic content, mg GAE 100 g−1
w.b.wet basis

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Published Online: 2017-2-9
Published in Print: 2017-4-1

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