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Effects of hot-air and hybrid hot air-microwave drying on drying kinetics and textural quality of nectarine slices
Drying and physicochemical characteristics of nectarine slices were investigated using hot-air and hybrid hot air-microwave drying methods under fixed air temperature and air speed (50 °C and 0.5 m/s, respectively). Microwave power levels for the combined hot air-microwave method were 80, 160, 240,...
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Published in: | Heat and mass transfer 2018-04, Vol.54 (4), p.915-927 |
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description | Drying and physicochemical characteristics of nectarine slices were investigated using hot-air and hybrid hot air-microwave drying methods under fixed air temperature and air speed (50 °C and 0.5 m/s, respectively). Microwave power levels for the combined hot air-microwave method were 80, 160, 240, and 320 W. Drying kinetics were analyzed and compared using six mathematical models. For both drying methods the model with the best fitness in explaining the drying behavior was the Midilli–Kucuk model. The coefficient of determination (
R
2
), root mean square error (RMSE) and reduced chi square (
χ
2
) for this model have been obtained greater than 0.999 and less than 0.006 and 0.0001 for hybrid hot air-microwave drying while those values for hot-air drying were more than 0.999 and less than 0.003 and 0.0001, respectively. Results showed that the hybrid method reduced the drying time considerably and produced products with higher quality. The range of effective moisture diffusivity (
D
eff
) of hybrid and hot-air drying was between 8.15 × 10
−8
and 2.83 × 10
−7
m
2
/s and 1.27 × 10
−8
m
2
/s, respectively. The total color difference (ΔE) has also been obtained from 36.68 to 44.27 for hybrid method; however this value for hot-air drying was found 49.64. Although reduced microwave power output led to a lower drying rate, it reduced changes in product parameters i.e. total color change, surface roughness, shrinkage and microstructural change and increased hardness and water uptake. |
doi_str_mv | 10.1007/s00231-017-2187-0 |
format | article |
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R
2
), root mean square error (RMSE) and reduced chi square (
χ
2
) for this model have been obtained greater than 0.999 and less than 0.006 and 0.0001 for hybrid hot air-microwave drying while those values for hot-air drying were more than 0.999 and less than 0.003 and 0.0001, respectively. Results showed that the hybrid method reduced the drying time considerably and produced products with higher quality. The range of effective moisture diffusivity (
D
eff
) of hybrid and hot-air drying was between 8.15 × 10
−8
and 2.83 × 10
−7
m
2
/s and 1.27 × 10
−8
m
2
/s, respectively. The total color difference (ΔE) has also been obtained from 36.68 to 44.27 for hybrid method; however this value for hot-air drying was found 49.64. Although reduced microwave power output led to a lower drying rate, it reduced changes in product parameters i.e. total color change, surface roughness, shrinkage and microstructural change and increased hardness and water uptake.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-017-2187-0</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Air drying ; Air temperature ; Chi-square test ; Color ; Engineering ; Engineering Thermodynamics ; Fitness ; Heat and Mass Transfer ; Industrial Chemistry/Chemical Engineering ; Mathematical models ; Original ; Root-mean-square errors ; Shrinkage ; Surface roughness ; Thermodynamics ; Water hardness</subject><ispartof>Heat and mass transfer, 2018-04, Vol.54 (4), p.915-927</ispartof><rights>Springer-Verlag GmbH Germany 2017</rights><rights>Copyright Springer Science & Business Media 2018</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c353t-f4acda326c88a2afd231cabea2a4f4d6218082d00c3f5bdad3e2d80da0ed6c133</citedby><cites>FETCH-LOGICAL-c353t-f4acda326c88a2afd231cabea2a4f4d6218082d00c3f5bdad3e2d80da0ed6c133</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Miraei Ashtiani, Seyed-Hassan</creatorcontrib><creatorcontrib>Sturm, Barbara</creatorcontrib><creatorcontrib>Nasirahmadi, Abozar</creatorcontrib><title>Effects of hot-air and hybrid hot air-microwave drying on drying kinetics and textural quality of nectarine slices</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>Drying and physicochemical characteristics of nectarine slices were investigated using hot-air and hybrid hot air-microwave drying methods under fixed air temperature and air speed (50 °C and 0.5 m/s, respectively). Microwave power levels for the combined hot air-microwave method were 80, 160, 240, and 320 W. Drying kinetics were analyzed and compared using six mathematical models. For both drying methods the model with the best fitness in explaining the drying behavior was the Midilli–Kucuk model. The coefficient of determination (
R
2
), root mean square error (RMSE) and reduced chi square (
χ
2
) for this model have been obtained greater than 0.999 and less than 0.006 and 0.0001 for hybrid hot air-microwave drying while those values for hot-air drying were more than 0.999 and less than 0.003 and 0.0001, respectively. Results showed that the hybrid method reduced the drying time considerably and produced products with higher quality. The range of effective moisture diffusivity (
D
eff
) of hybrid and hot-air drying was between 8.15 × 10
−8
and 2.83 × 10
−7
m
2
/s and 1.27 × 10
−8
m
2
/s, respectively. The total color difference (ΔE) has also been obtained from 36.68 to 44.27 for hybrid method; however this value for hot-air drying was found 49.64. Although reduced microwave power output led to a lower drying rate, it reduced changes in product parameters i.e. total color change, surface roughness, shrinkage and microstructural change and increased hardness and water uptake.</description><subject>Air drying</subject><subject>Air temperature</subject><subject>Chi-square test</subject><subject>Color</subject><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Fitness</subject><subject>Heat and Mass Transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Mathematical models</subject><subject>Original</subject><subject>Root-mean-square errors</subject><subject>Shrinkage</subject><subject>Surface roughness</subject><subject>Thermodynamics</subject><subject>Water hardness</subject><issn>0947-7411</issn><issn>1432-1181</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp1kEtPwzAQhC0EEqXwA7hZ4mxYP5qEI6rKQ6rEBc6W60frkiat7QD59zgExInTrlbfzGoGoUsK1xSgvIkAjFMCtCSMViWBIzShgjNCaUWP0QRuRUlKQekpOotxm-lCMD5BYeGc1Sni1uFNm4jyAavG4E2_Ct4MJ5xPZOd1aD_Uu8Um9L5Z47b53d58Y5PX8VuW7GfqgqrxoVO1T_1g22R_FTKFY-21jefoxKk62oufOUWv94uX-SNZPj88ze-WRPMZT8QJpY3irNBVpZhyJufTamXzLpwwRY4JFTMAmrvZyijDLTMVGAXWFJpyPkVXo-8-tIfOxiS3bRea_FIyoKIUMCsGio5UDhhjsE7ug9-p0EsKcqhWjtXKXK0cqpWQNWzUxMw2axv-nP8XfQFFM34j</recordid><startdate>20180401</startdate><enddate>20180401</enddate><creator>Miraei Ashtiani, Seyed-Hassan</creator><creator>Sturm, Barbara</creator><creator>Nasirahmadi, Abozar</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20180401</creationdate><title>Effects of hot-air and hybrid hot air-microwave drying on drying kinetics and textural quality of nectarine slices</title><author>Miraei Ashtiani, Seyed-Hassan ; Sturm, Barbara ; Nasirahmadi, Abozar</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c353t-f4acda326c88a2afd231cabea2a4f4d6218082d00c3f5bdad3e2d80da0ed6c133</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Air drying</topic><topic>Air temperature</topic><topic>Chi-square test</topic><topic>Color</topic><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Fitness</topic><topic>Heat and Mass Transfer</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Mathematical models</topic><topic>Original</topic><topic>Root-mean-square errors</topic><topic>Shrinkage</topic><topic>Surface roughness</topic><topic>Thermodynamics</topic><topic>Water hardness</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Miraei Ashtiani, Seyed-Hassan</creatorcontrib><creatorcontrib>Sturm, Barbara</creatorcontrib><creatorcontrib>Nasirahmadi, Abozar</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Miraei Ashtiani, Seyed-Hassan</au><au>Sturm, Barbara</au><au>Nasirahmadi, Abozar</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Effects of hot-air and hybrid hot air-microwave drying on drying kinetics and textural quality of nectarine slices</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2018-04-01</date><risdate>2018</risdate><volume>54</volume><issue>4</issue><spage>915</spage><epage>927</epage><pages>915-927</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>Drying and physicochemical characteristics of nectarine slices were investigated using hot-air and hybrid hot air-microwave drying methods under fixed air temperature and air speed (50 °C and 0.5 m/s, respectively). Microwave power levels for the combined hot air-microwave method were 80, 160, 240, and 320 W. Drying kinetics were analyzed and compared using six mathematical models. For both drying methods the model with the best fitness in explaining the drying behavior was the Midilli–Kucuk model. The coefficient of determination (
R
2
), root mean square error (RMSE) and reduced chi square (
χ
2
) for this model have been obtained greater than 0.999 and less than 0.006 and 0.0001 for hybrid hot air-microwave drying while those values for hot-air drying were more than 0.999 and less than 0.003 and 0.0001, respectively. Results showed that the hybrid method reduced the drying time considerably and produced products with higher quality. The range of effective moisture diffusivity (
D
eff
) of hybrid and hot-air drying was between 8.15 × 10
−8
and 2.83 × 10
−7
m
2
/s and 1.27 × 10
−8
m
2
/s, respectively. The total color difference (ΔE) has also been obtained from 36.68 to 44.27 for hybrid method; however this value for hot-air drying was found 49.64. Although reduced microwave power output led to a lower drying rate, it reduced changes in product parameters i.e. total color change, surface roughness, shrinkage and microstructural change and increased hardness and water uptake.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-017-2187-0</doi><tpages>13</tpages></addata></record> |
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subjects | Air drying Air temperature Chi-square test Color Engineering Engineering Thermodynamics Fitness Heat and Mass Transfer Industrial Chemistry/Chemical Engineering Mathematical models Original Root-mean-square errors Shrinkage Surface roughness Thermodynamics Water hardness |
title | Effects of hot-air and hybrid hot air-microwave drying on drying kinetics and textural quality of nectarine slices |
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