Thin layer drying of zucchini in solar dryer located in Osmaniye region

In this study, the dehydration behavior of zucchini using solar assisted drying system was examined according to 22 thin layer drying models available in literature. The correlation coefficient (R2), chi-square (χ2) and root mean square error (RMSE) values were calculated to check the suitability of...

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Main Authors: Özge Süfer, Mustafa Söyler, Coşkun Özalp, Kamil Neyfel Çerçi, Ertaç Hürdoğan
Format: Article
Language:English
Published: University North 2018-01-01
Series:Tehnički Glasnik
Subjects:
Online Access:https://hrcak.srce.hr/file/297860
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spelling doaj-bf99e30b07424bfd88d24f9e36a38c272020-11-25T00:19:35ZengUniversity NorthTehnički Glasnik1846-61681848-55882018-01-011227985Thin layer drying of zucchini in solar dryer located in Osmaniye regionÖzge Süfer0Mustafa Söyler1Coşkun Özalp2Kamil Neyfel Çerçi3Ertaç Hürdoğan4Department of Food Engineering, Osmaniye Korkut Ata University, Osmaniye, TurkeyDepartment of Energy Systems Engineering, Osmaniye Korkut Ata University, Osmaniye, TurkeyDepartment of Energy Systems Engineering, Osmaniye Korkut Ata University, Osmaniye, TurkeyDepartment of Energy Systems Engineering, Osmaniye Korkut Ata University, Osmaniye, TurkeyDepartment of Energy Systems Engineering, Osmaniye Korkut Ata University, Osmaniye, TurkeyIn this study, the dehydration behavior of zucchini using solar assisted drying system was examined according to 22 thin layer drying models available in literature. The correlation coefficient (R2), chi-square (χ2) and root mean square error (RMSE) values were calculated to check the suitability of models by non-linear regression analysis. It was found that Cubic and Modified Midilli-1 models were the most suitable equations and their R2 values were calculated as 0.99963. χ2 and RMSE values of related mathematical expressions were 1.89343×10‒5, 1.91692×10‒5 and 0.01685×10‒3, 0.01721×10‒3 respectively. In addition, heat transfer, mass transfer and diffusion coefficients, which were important parameters in design of drying systems were also determined as 5.18124 W/m2°C, 1.57129×10‒7 m/s and 2.335718×10‒9 m2/s respectively.https://hrcak.srce.hr/file/297860diffusion coefficientheat and mass transfer coefficientmathematical modeling
collection DOAJ
language English
format Article
sources DOAJ
author Özge Süfer
Mustafa Söyler
Coşkun Özalp
Kamil Neyfel Çerçi
Ertaç Hürdoğan
spellingShingle Özge Süfer
Mustafa Söyler
Coşkun Özalp
Kamil Neyfel Çerçi
Ertaç Hürdoğan
Thin layer drying of zucchini in solar dryer located in Osmaniye region
Tehnički Glasnik
diffusion coefficient
heat and mass transfer coefficient
mathematical modeling
author_facet Özge Süfer
Mustafa Söyler
Coşkun Özalp
Kamil Neyfel Çerçi
Ertaç Hürdoğan
author_sort Özge Süfer
title Thin layer drying of zucchini in solar dryer located in Osmaniye region
title_short Thin layer drying of zucchini in solar dryer located in Osmaniye region
title_full Thin layer drying of zucchini in solar dryer located in Osmaniye region
title_fullStr Thin layer drying of zucchini in solar dryer located in Osmaniye region
title_full_unstemmed Thin layer drying of zucchini in solar dryer located in Osmaniye region
title_sort thin layer drying of zucchini in solar dryer located in osmaniye region
publisher University North
series Tehnički Glasnik
issn 1846-6168
1848-5588
publishDate 2018-01-01
description In this study, the dehydration behavior of zucchini using solar assisted drying system was examined according to 22 thin layer drying models available in literature. The correlation coefficient (R2), chi-square (χ2) and root mean square error (RMSE) values were calculated to check the suitability of models by non-linear regression analysis. It was found that Cubic and Modified Midilli-1 models were the most suitable equations and their R2 values were calculated as 0.99963. χ2 and RMSE values of related mathematical expressions were 1.89343×10‒5, 1.91692×10‒5 and 0.01685×10‒3, 0.01721×10‒3 respectively. In addition, heat transfer, mass transfer and diffusion coefficients, which were important parameters in design of drying systems were also determined as 5.18124 W/m2°C, 1.57129×10‒7 m/s and 2.335718×10‒9 m2/s respectively.
topic diffusion coefficient
heat and mass transfer coefficient
mathematical modeling
url https://hrcak.srce.hr/file/297860
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AT mustafasoyler thinlayerdryingofzucchiniinsolardryerlocatedinosmaniyeregion
AT coskunozalp thinlayerdryingofzucchiniinsolardryerlocatedinosmaniyeregion
AT kamilneyfelcerci thinlayerdryingofzucchiniinsolardryerlocatedinosmaniyeregion
AT ertachurdogan thinlayerdryingofzucchiniinsolardryerlocatedinosmaniyeregion
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