Drying kinetics of onion (Allium cepa L.) slices with convective and microwave drying
Onion slices were dried using two different drying techniques, convective and microwave drying. Convective drying treatments were carried out at different temperatures (50, 60 and 70 °C). Three different microwave output powers 328, 447 and 557 W were used in microwave drying. In convective drying,...
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creator | Demiray, Engin Seker, Anıl Tulek, Yahya |
description | Onion slices were dried using two different drying techniques, convective and microwave drying. Convective drying treatments were carried out at different temperatures (50, 60 and 70 °C). Three different microwave output powers 328, 447 and 557 W were used in microwave drying. In convective drying, effective moisture diffusivity was estimated to be between 3.49 × 10
−8
and 9.44 × 10
−8
m
2
s
−1
within the temperature range studied. The effect of temperature on the diffusivity was described by the Arrhenius equation with an activation energy of 45.60 kJ mol
−1
. At increasing microwave power values, the effective moisture diffusivity values ranged from 2.59 × 10
−7
and 5.08 × 10
−8
m
2
s
−1
. The activation energy for microwave drying of samples was calculated using an exponential expression based on Arrhenius equation. Among of the models proposed, Page’s model gave a better fit for all drying conditions used. |
doi_str_mv | 10.1007/s00231-016-1943-x |
format | Article |
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−8
and 9.44 × 10
−8
m
2
s
−1
within the temperature range studied. The effect of temperature on the diffusivity was described by the Arrhenius equation with an activation energy of 45.60 kJ mol
−1
. At increasing microwave power values, the effective moisture diffusivity values ranged from 2.59 × 10
−7
and 5.08 × 10
−8
m
2
s
−1
. The activation energy for microwave drying of samples was calculated using an exponential expression based on Arrhenius equation. Among of the models proposed, Page’s model gave a better fit for all drying conditions used.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-016-1943-x</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Activation energy ; Convective drying ; Diffusivity ; Engineering ; Engineering Thermodynamics ; Heat and Mass Transfer ; Industrial Chemistry/Chemical Engineering ; Moisture ; Onions ; Original ; Temperature ; Temperature effects ; Thermodynamics</subject><ispartof>Heat and mass transfer, 2017-05, Vol.53 (5), p.1817-1827</ispartof><rights>Springer-Verlag Berlin Heidelberg 2016</rights><rights>Copyright Springer Science & Business Media 2017</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c316t-aeb4bfcd922420027322919997a3bcaaaa3d4e223cf78edfe5dcfde731ca2c723</citedby><cites>FETCH-LOGICAL-c316t-aeb4bfcd922420027322919997a3bcaaaa3d4e223cf78edfe5dcfde731ca2c723</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s00231-016-1943-x$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s00231-016-1943-x$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27901,27902,41464,42533,51294</link.rule.ids></links><search><creatorcontrib>Demiray, Engin</creatorcontrib><creatorcontrib>Seker, Anıl</creatorcontrib><creatorcontrib>Tulek, Yahya</creatorcontrib><title>Drying kinetics of onion (Allium cepa L.) slices with convective and microwave drying</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>Onion slices were dried using two different drying techniques, convective and microwave drying. Convective drying treatments were carried out at different temperatures (50, 60 and 70 °C). Three different microwave output powers 328, 447 and 557 W were used in microwave drying. In convective drying, effective moisture diffusivity was estimated to be between 3.49 × 10
−8
and 9.44 × 10
−8
m
2
s
−1
within the temperature range studied. The effect of temperature on the diffusivity was described by the Arrhenius equation with an activation energy of 45.60 kJ mol
−1
. At increasing microwave power values, the effective moisture diffusivity values ranged from 2.59 × 10
−7
and 5.08 × 10
−8
m
2
s
−1
. The activation energy for microwave drying of samples was calculated using an exponential expression based on Arrhenius equation. Among of the models proposed, Page’s model gave a better fit for all drying conditions used.</description><subject>Activation energy</subject><subject>Convective drying</subject><subject>Diffusivity</subject><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Heat and Mass Transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Moisture</subject><subject>Onions</subject><subject>Original</subject><subject>Temperature</subject><subject>Temperature effects</subject><subject>Thermodynamics</subject><issn>0947-7411</issn><issn>1432-1181</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNp1kDtPAzEQhC0EEiHwA-gs0UDh4LXN-a6MwlOKRENqy_H5gsPFDvbl9e8xHAUN26xW-mZ2NAhdAh0BpfI2Uco4EAoFgUpwsj9CAxCcEYASjtGAVkISKQBO0VlKy0wXgvEBmt3Hg_ML_OG87ZxJODQ4eBc8vh63rdussLFrjaejG5xaZ2zCO9e9YxP81prObS3WvsYrZ2LY6XzVP3bn6KTRbbIXv3uIZo8Pb5NnMn19epmMp8RwKDqi7VzMG1NXjAmWI0nOWAVVVUnN50bn4bWwjHHTyNLWjb2rTVNbycFoZiTjQ3TV-65j-NzY1Kll2ESfXyooS0kLzkuZKeipHDKlaBu1jm6l40EBVd_tqb49ldtT3-2pfdawXpMy6xc2_nH-V_QFkARzHQ</recordid><startdate>20170501</startdate><enddate>20170501</enddate><creator>Demiray, Engin</creator><creator>Seker, Anıl</creator><creator>Tulek, Yahya</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20170501</creationdate><title>Drying kinetics of onion (Allium cepa L.) slices with convective and microwave drying</title><author>Demiray, Engin ; Seker, Anıl ; Tulek, Yahya</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c316t-aeb4bfcd922420027322919997a3bcaaaa3d4e223cf78edfe5dcfde731ca2c723</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Activation energy</topic><topic>Convective drying</topic><topic>Diffusivity</topic><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Heat and Mass Transfer</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Moisture</topic><topic>Onions</topic><topic>Original</topic><topic>Temperature</topic><topic>Temperature effects</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Demiray, Engin</creatorcontrib><creatorcontrib>Seker, Anıl</creatorcontrib><creatorcontrib>Tulek, Yahya</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Demiray, Engin</au><au>Seker, Anıl</au><au>Tulek, Yahya</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Drying kinetics of onion (Allium cepa L.) slices with convective and microwave drying</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2017-05-01</date><risdate>2017</risdate><volume>53</volume><issue>5</issue><spage>1817</spage><epage>1827</epage><pages>1817-1827</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>Onion slices were dried using two different drying techniques, convective and microwave drying. Convective drying treatments were carried out at different temperatures (50, 60 and 70 °C). Three different microwave output powers 328, 447 and 557 W were used in microwave drying. In convective drying, effective moisture diffusivity was estimated to be between 3.49 × 10
−8
and 9.44 × 10
−8
m
2
s
−1
within the temperature range studied. The effect of temperature on the diffusivity was described by the Arrhenius equation with an activation energy of 45.60 kJ mol
−1
. At increasing microwave power values, the effective moisture diffusivity values ranged from 2.59 × 10
−7
and 5.08 × 10
−8
m
2
s
−1
. The activation energy for microwave drying of samples was calculated using an exponential expression based on Arrhenius equation. Among of the models proposed, Page’s model gave a better fit for all drying conditions used.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-016-1943-x</doi><tpages>11</tpages></addata></record> |
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subjects | Activation energy Convective drying Diffusivity Engineering Engineering Thermodynamics Heat and Mass Transfer Industrial Chemistry/Chemical Engineering Moisture Onions Original Temperature Temperature effects Thermodynamics |
title | Drying kinetics of onion (Allium cepa L.) slices with convective and microwave drying |
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