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Articles

Research on the drying kinetics of household food waste for the development and optimization of domestic waste drying technique

, , , &
Pages 929-939
Received 16 Mar 2015
Accepted 03 Sep 2015
Accepted author version posted online: 28 Oct 2015
Published online: 20 Nov 2015

ABSTRACT

Domestic food waste drying foresees the significant reduction of household food waste mass through the hygienic removal of its moisture content at source. In this manuscript, a new approach for the development and optimization of an innovative household waste dryer for the effective dehydration of food waste at source is presented. Food waste samples were dehydrated with the use of the heated air-drying technique under different air-drying conditions, namely air temperature and air velocity, in order to investigate their drying kinetics. Different thin-layer drying models have been applied, in which the drying constant is a function of the process variables. The Midilli model demonstrated the best performance in fitting the experimental data in all tested samples, whereas it was found that food waste drying is greatly affected by temperature and to a smaller scale by air velocity. Due to the increased moisture content of food waste, an appropriate configuration of the drying process variables can lead to a total reduction of its mass by 87% w/w, thus achieving a sustainable residence time and energy consumption level. Thus, the development of a domestic waste dryer can be proved to be economically and environmentally viable in the future.

Acknowledgements

This work is based on the research that was carried out in the framework of a LIFE+ project entitled: ‘Development and demonstration of an innovative household dryer for the treatment of organic waste,’ DRYWASTE, (LIFE08 ENV/GR/000566, 2010–2012), which was co-financed by the European Commission.

Disclosure statement

No potential conflict of interest was reported by the authors.

Nomenclature

MR

moisture ratio

k, k′, k

drying rate constants (min−1)

k0, k1, k2, k3

empirical drying coefficients (min−1)

a, b, c, d, g, h, n

coefficients

t

drying time (min)

Xe

equilibrium moisture content (kg H2O/kg dry matter)

X0

initial moisture content (kg H2O/kg dry matter)

Xt

moisture content at time t (kg H2O / kg dry matter)

T

air temperature (oC)

V

air flow velocity (m/s)

RH

relative humidity (%)

L

sample particle dimension (mm)

Xexp,i

ith experimentally observed moisture content

Xcalc,i

ith calculated moisture content

N

number of observations

RMSE

root mean square error

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