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Unripe Banana Flour Produced by Air-Drying Assisted with Ultrasound – Description of the Mechanisms Involved to Enhance the Mass Transfer in Two Approaches

  • Carla I.A. La Fuente and Carmen C. Tadini EMAIL logo
Published/Copyright: November 16, 2017

Abstract

In this research the application of ultrasound, prior to air-drying, describing the phenomena in two approaches: unripe banana slices immersed in water (hydrated) and vacuum packaged (non-hydrated) were investigated. The results showed two falling rate periods during the air-drying. For the second rate period, an increase of water effective diffusivity due to the “sponge effect” (direct effect of ultrasound) and the microscopic channels formation (indirect effect) was observed. Scanning electron microscopy images showed that untreated dried slices were less porous, characterized by small cavities and high density, while ultrasound pretreated slices resulted in a porous structure with more free volume between cells. An increase in porosity decreased the resistance for diffusion, influencing positively the water effective diffusivity. Moreover, ultrasound produced partial disorder of the crystalline structure within the starch granules, reducing the amount of energy required for gelatinization. Moreover, reduction of resistant starch content was not observed.

Funding statement: The authors acknowledge financial support from the São Paulo Research Foundation (FAPESP) under grants 2011/22398-0 and 2013/07914-8, the scholarship provided by the Coordination for the Improvement of Higher Education Personnel (CAPES) and by CNPq (National Council for Scientific and Technological Development) under grant 306440/2013-0. Thanks for Prof. Elizabete Wenzel de Menezes and Aline de Oliveira Santos (Dept. of Food and Experimental Nutrition, Faculty of Pharmaceutical Sciences, University of São Paulo), for help with resistant starch analyses.

Nomenclature

a

constant of Logarithmic and Midilli’s models (-)

aw

water activity (-)

b

constant of Midilli’s model (1/min)

c

constant of Logarithmic model (-)

Cp

specific heat (J/g K)

Deff

water effective diffusivity (m2/s)

k

drying kinetic parameter of Logarithmic and Midilli’s models (1/min)

L

sample half-thickness (m)

m

mass (g)

MR

moisture ratio (-)

n

constant of Midilli’s model (-)

PUS

ultrasonic volumetric power (W/L)

RH

relative humidity (%)

RS

resistant starch content (g /100 g d.b.)

S

solubility (g/100 g)

t

time (min)

T

temperature (°C)

V

volume (L)

x

moisture content on wet basis (g H2O/g)

X

moisture content on dry basis (g H2O/g)

WG

water gain (g/100 g)

Subscripts

0

Initial

e

Equilibrium

f

Flour

p

Peak

US

ultrasound

Greek letter

ΔH

gelatinization enthalpy (J/g)

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Received: 2017-6-1
Accepted: 2017-10-11
Published Online: 2017-11-16

© 2017 Walter de Gruyter GmbH, Berlin/Boston

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