Drying kinetics of apricot halves in a microwave-hot air hybrid oven
Drying behavior and kinetics of apricot halves were investigated in a microwave-hot air domestic hybrid oven at 120, 150 and 180 W microwave power and 50, 60 and 70 °C air temperature. Drying operation was finished when the moisture content reached to 25% (wet basis) from 77% (w.b). Increase in micr...
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description | Drying behavior and kinetics of apricot halves were investigated in a microwave-hot air domestic hybrid oven at 120, 150 and 180 W microwave power and 50, 60 and 70 °C air temperature. Drying operation was finished when the moisture content reached to 25% (wet basis) from 77% (w.b). Increase in microwave power and air temperature increased drying rates and reduced drying time. Only falling rate period was observed in drying of apricot halves in hybrid oven. Eleven mathematical models were used for describing the drying kinetics of apricots. Modified logistic model gave the best fitting to the experimental data. The model has never been used to explain drying behavior of any kind of food materials up to now. Fick’s second law was used for determination of both effective moisture diffusivity and thermal diffusivity values. Activation energy values of dried apricots were calculated from Arrhenius equation. Those that obtained from effective moisture diffusivity, thermal diffusivity and drying rate constant values ranged from 31.10 to 39.4 kJ/mol, 29.56 to 35.19 kJ/mol, and 26.02 to 32.36 kJ/mol, respectively. |
doi_str_mv | 10.1007/s00231-017-1973-z |
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Drying operation was finished when the moisture content reached to 25% (wet basis) from 77% (w.b). Increase in microwave power and air temperature increased drying rates and reduced drying time. Only falling rate period was observed in drying of apricot halves in hybrid oven. Eleven mathematical models were used for describing the drying kinetics of apricots. Modified logistic model gave the best fitting to the experimental data. The model has never been used to explain drying behavior of any kind of food materials up to now. Fick’s second law was used for determination of both effective moisture diffusivity and thermal diffusivity values. Activation energy values of dried apricots were calculated from Arrhenius equation. Those that obtained from effective moisture diffusivity, thermal diffusivity and drying rate constant values ranged from 31.10 to 39.4 kJ/mol, 29.56 to 35.19 kJ/mol, and 26.02 to 32.36 kJ/mol, respectively.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-017-1973-z</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Air temperature ; Apricots ; Diffusivity ; Drying ovens ; Energy value ; Engineering ; Engineering Thermodynamics ; Heat and Mass Transfer ; High temperature air ; Industrial Chemistry/Chemical Engineering ; Kinetics ; Moisture content ; Original ; Thermal diffusivity ; Thermodynamics</subject><ispartof>Heat and mass transfer, 2017-06, Vol.53 (6), p.2117-2127</ispartof><rights>Springer-Verlag Berlin Heidelberg 2017</rights><rights>Copyright Springer Science & Business Media 2017</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c316t-e1214c60597179e964c9c33cbdf4ddb60c9a8392cd718d545b49839f475080f13</citedby><cites>FETCH-LOGICAL-c316t-e1214c60597179e964c9c33cbdf4ddb60c9a8392cd718d545b49839f475080f13</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/s00231-017-1973-z$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s00231-017-1973-z$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27923,27924,41487,42556,51318</link.rule.ids></links><search><creatorcontrib>Horuz, Erhan</creatorcontrib><creatorcontrib>Bozkurt, Hüseyin</creatorcontrib><creatorcontrib>Karataş, Haluk</creatorcontrib><creatorcontrib>Maskan, Medeni</creatorcontrib><title>Drying kinetics of apricot halves in a microwave-hot air hybrid oven</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>Drying behavior and kinetics of apricot halves were investigated in a microwave-hot air domestic hybrid oven at 120, 150 and 180 W microwave power and 50, 60 and 70 °C air temperature. Drying operation was finished when the moisture content reached to 25% (wet basis) from 77% (w.b). Increase in microwave power and air temperature increased drying rates and reduced drying time. Only falling rate period was observed in drying of apricot halves in hybrid oven. Eleven mathematical models were used for describing the drying kinetics of apricots. Modified logistic model gave the best fitting to the experimental data. The model has never been used to explain drying behavior of any kind of food materials up to now. Fick’s second law was used for determination of both effective moisture diffusivity and thermal diffusivity values. Activation energy values of dried apricots were calculated from Arrhenius equation. Those that obtained from effective moisture diffusivity, thermal diffusivity and drying rate constant values ranged from 31.10 to 39.4 kJ/mol, 29.56 to 35.19 kJ/mol, and 26.02 to 32.36 kJ/mol, respectively.</description><subject>Air temperature</subject><subject>Apricots</subject><subject>Diffusivity</subject><subject>Drying ovens</subject><subject>Energy value</subject><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Heat and Mass Transfer</subject><subject>High temperature air</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Kinetics</subject><subject>Moisture content</subject><subject>Original</subject><subject>Thermal diffusivity</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>eNp1kDFPwzAQhS0EEqXwA9gsMRvuYieOR9RCQarEArPlOE7r0ibFTovaX4-rMLAwnU73vXd3j5BbhHsEkA8RIOPIACVDJTk7npERCp4xxBLPyQiUkEwKxEtyFeMq0YXI-IhMp-Hg2wX99K3rvY20a6jZBm-7ni7Neu8i9S01dONt6L7N3rFlmhgf6PJQBV_Tbu_aa3LRmHV0N791TD6en94nL2z-NnudPM6Z5Vj0zGGGwhaQK4lSOVUIqyzntqobUddVAVaZkqvM1hLLOhd5JVTqGyFzKKFBPiZ3g-82dF87F3u96nahTSs1KgAuy1JBonCg0sUxBtfo9M_GhING0Kew9BCWTmHpU1j6mDTZoImJbRcu_HH-V_QDTYproQ</recordid><startdate>20170601</startdate><enddate>20170601</enddate><creator>Horuz, Erhan</creator><creator>Bozkurt, Hüseyin</creator><creator>Karataş, Haluk</creator><creator>Maskan, Medeni</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20170601</creationdate><title>Drying kinetics of apricot halves in a microwave-hot air hybrid oven</title><author>Horuz, Erhan ; Bozkurt, Hüseyin ; Karataş, Haluk ; Maskan, Medeni</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c316t-e1214c60597179e964c9c33cbdf4ddb60c9a8392cd718d545b49839f475080f13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Air temperature</topic><topic>Apricots</topic><topic>Diffusivity</topic><topic>Drying ovens</topic><topic>Energy value</topic><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Heat and Mass Transfer</topic><topic>High temperature air</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Kinetics</topic><topic>Moisture content</topic><topic>Original</topic><topic>Thermal diffusivity</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Horuz, Erhan</creatorcontrib><creatorcontrib>Bozkurt, Hüseyin</creatorcontrib><creatorcontrib>Karataş, Haluk</creatorcontrib><creatorcontrib>Maskan, Medeni</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Horuz, Erhan</au><au>Bozkurt, Hüseyin</au><au>Karataş, Haluk</au><au>Maskan, Medeni</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Drying kinetics of apricot halves in a microwave-hot air hybrid oven</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2017-06-01</date><risdate>2017</risdate><volume>53</volume><issue>6</issue><spage>2117</spage><epage>2127</epage><pages>2117-2127</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>Drying behavior and kinetics of apricot halves were investigated in a microwave-hot air domestic hybrid oven at 120, 150 and 180 W microwave power and 50, 60 and 70 °C air temperature. Drying operation was finished when the moisture content reached to 25% (wet basis) from 77% (w.b). Increase in microwave power and air temperature increased drying rates and reduced drying time. Only falling rate period was observed in drying of apricot halves in hybrid oven. Eleven mathematical models were used for describing the drying kinetics of apricots. Modified logistic model gave the best fitting to the experimental data. The model has never been used to explain drying behavior of any kind of food materials up to now. Fick’s second law was used for determination of both effective moisture diffusivity and thermal diffusivity values. Activation energy values of dried apricots were calculated from Arrhenius equation. Those that obtained from effective moisture diffusivity, thermal diffusivity and drying rate constant values ranged from 31.10 to 39.4 kJ/mol, 29.56 to 35.19 kJ/mol, and 26.02 to 32.36 kJ/mol, respectively.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-017-1973-z</doi><tpages>11</tpages></addata></record> |
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subjects | Air temperature Apricots Diffusivity Drying ovens Energy value Engineering Engineering Thermodynamics Heat and Mass Transfer High temperature air Industrial Chemistry/Chemical Engineering Kinetics Moisture content Original Thermal diffusivity Thermodynamics |
title | Drying kinetics of apricot halves in a microwave-hot air hybrid oven |
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