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Drying characteristics of jujube (Zizyphus jujuba) slices in a hot air dryer and physicochemical properties of jujube powder

  • Feyza Elmas
  • Emine Varhan
  • Mehmet KoçEmail author
Original Paper

Abstract

The hot air convective drying characteristics of sliced jujube fruits were investigated. Drying experiments were carried out at three different temperatures (60, 70 and 80 °C) and three different air velocity (0.5, 1.0, 1.5 m·s−1). All drying experiments had only falling rate period. The average effective diffusivity values varied from 1.2 × 10−9 to 3.55 × 10−9 m2·s−1 over the temperature and velocity range studied and the activation energy was estimated to be 28.183 kJ·mol−1 by modified Arrhenius Equation. In order to select a suitable form of the drying curve, seven different thin layer drying model was investigated and Page and Wangh and Singh models were considered the best to explain the drying of the jujube slices. Also, the influence of varied drying temperatures and velocity were investigated on physicochemical properties of the jujube powder. It was observed that moisture content and water activity values, which are an important powder product property, decrease with increasing temperature. It was found that the powder product obtained has different particle properties depending on the air temperature and velocity and therefore has different bulk and reconstitution properties. Within the scope of chemical analyzes, it was observed that the sugar content of the powder products is considerably high due to low moisture content. Also, according to the total phenolic content analysis, the higher temperature resulted in the lower total phenolic content.

Keywords

Jujube Powder Drying kinetic Hot air drying Flowability Sugar content 

Abbreviations

SMIR

Short-medium infrared drying

HA

Hot air drying

X

Moisture content (kg water·kg dry matter−1)

MR

Dimensionless moisture content

Bimass

Biot number

De

Effective diffusivity (m2·s−1)

z

Distance for diffusion (m).

t

Drying time (s).

X0

Initial moisture content (kg water·kg dry matter−1)

Xs

Surface moisture content (kg water·kg dry matter−1)

Xe

Equilibrium moisture content (kg water·kg dry matter−1)

kc

Convective mass transfer coefficient (m·s−1)

L

Thickness of slab (m)

D0

Pre-exponential factor of the Arrhenius equation (m2·s−1)

Ea

Activation energy (kJ·mol−1)

R

Universal gas constant (kJ·mol−1·K−1)

T

Absolute air temperature (K)

V

Velocity of dryer air (m·s−1)

RMSE

Root mean square error

D[4,3]

De Brouckere mean diameter

ms

Pycnometer weight (g) filled with powder product

m0

Empty pycnometer weight (g)

ρ

Density of 2-propanol (0.785 g·ml−1)

ρp

Particle density of powder (kg m−3)

ml

Pycnometer weight filled with 2-propanol (g)

msl

Pycnometer weight filled powder product and 2-propanol (g)

ρb

Bulk density of powder (kg.m−3)

ρt

Tapped density of powder (kg.m−3)

CI

Carr index

RID

Refractive index detector

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Copyright information

© Springer Science+Business Media, LLC, part of Springer Nature 2018

Authors and Affiliations

  1. 1.Department of Food Engineering, Faculty of EngineeringAdnan Menderes UniversityAydınTurkey

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