Deacidification of sulfur olive oil. II. Multi-stage liquid-liquid extraction of miscella with ethyl alcohol
In this study, laboratory‐scale multi‐stage cross‐ and counter‐current extractions of sulfur olive oil miscella with 70 and 80% ethanol saturated with hexane were investigated. For cross‐current extraction, the extraction factor for free fatty acids was constant in each extraction stage. Therefore,...
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Veröffentlicht in: | Journal of the American Oil Chemists' Society 1991-11, Vol.68 (11), p.818-821 |
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creator | Turkay, S. (Technical University of Istanbul, Istanbul, Turkey) Civelekoglu, H |
description | In this study, laboratory‐scale multi‐stage cross‐ and counter‐current extractions of sulfur olive oil miscella with 70 and 80% ethanol saturated with hexane were investigated. For cross‐current extraction, the extraction factor for free fatty acids was constant in each extraction stage. Therefore, the extraction factors determined in single‐stage extractions were used to calculate the extracted free fatty acid percentages for cross‐current and counter‐current multi‐stage extractions and results were in close agreement with the experimental data. It was possible to determine the amount of solvent and the number of stages required for counter‐current extraction to remove the desired amount of free fatty acids from a given sulfur olive oil with 70 or 80% ethanol. Comparison of the results for these two solvents showed that 80% ethanol was more suitable. |
doi_str_mv | 10.1007/BF02660594 |
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Multi-stage liquid-liquid extraction of miscella with ethyl alcohol</title><source>Springer Nature - Complete Springer Journals</source><creator>Turkay, S. (Technical University of Istanbul, Istanbul, Turkey) ; Civelekoglu, H</creator><creatorcontrib>Turkay, S. (Technical University of Istanbul, Istanbul, Turkey) ; Civelekoglu, H</creatorcontrib><description>In this study, laboratory‐scale multi‐stage cross‐ and counter‐current extractions of sulfur olive oil miscella with 70 and 80% ethanol saturated with hexane were investigated. For cross‐current extraction, the extraction factor for free fatty acids was constant in each extraction stage. Therefore, the extraction factors determined in single‐stage extractions were used to calculate the extracted free fatty acid percentages for cross‐current and counter‐current multi‐stage extractions and results were in close agreement with the experimental data. It was possible to determine the amount of solvent and the number of stages required for counter‐current extraction to remove the desired amount of free fatty acids from a given sulfur olive oil with 70 or 80% ethanol. Comparison of the results for these two solvents showed that 80% ethanol was more suitable.</description><identifier>ISSN: 0003-021X</identifier><identifier>EISSN: 1558-9331</identifier><identifier>DOI: 10.1007/BF02660594</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer-Verlag</publisher><subject>ACEITUNA ; ACIDE GRAS ; ACIDOS GRASOS ; BYPRODUCTS ; Deacidification ; ETANOL ; ETHANOL ; FATTY ACIDS ; liquid‐liquid extraction ; OILSEED CAKES ; OLIVE ; OLIVE CAKE ; OLIVES ; PROCESAMIENTO ; PROCESSING ; refining ; SOUS PRODUIT ; SUBPRODUCTOS ; sulfur olive oil ; TORTAS OLEAGINOSAS ; TOURTEAU D'OLEAGINEUX ; TRAITEMENT ; TURKEY ; TURQUIA ; TURQUIE</subject><ispartof>Journal of the American Oil Chemists' Society, 1991-11, Vol.68 (11), p.818-821</ispartof><rights>1991 American Oil Chemists' Society (AOCS)</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c2048-36bc8d9cbb5d58142d960acb14f3982042c1d01d1f3864621ceed39c638f3da63</citedby><cites>FETCH-LOGICAL-c2048-36bc8d9cbb5d58142d960acb14f3982042c1d01d1f3864621ceed39c638f3da63</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27903,27904</link.rule.ids></links><search><creatorcontrib>Turkay, S. (Technical University of Istanbul, Istanbul, Turkey)</creatorcontrib><creatorcontrib>Civelekoglu, H</creatorcontrib><title>Deacidification of sulfur olive oil. II. Multi-stage liquid-liquid extraction of miscella with ethyl alcohol</title><title>Journal of the American Oil Chemists' Society</title><description>In this study, laboratory‐scale multi‐stage cross‐ and counter‐current extractions of sulfur olive oil miscella with 70 and 80% ethanol saturated with hexane were investigated. For cross‐current extraction, the extraction factor for free fatty acids was constant in each extraction stage. Therefore, the extraction factors determined in single‐stage extractions were used to calculate the extracted free fatty acid percentages for cross‐current and counter‐current multi‐stage extractions and results were in close agreement with the experimental data. It was possible to determine the amount of solvent and the number of stages required for counter‐current extraction to remove the desired amount of free fatty acids from a given sulfur olive oil with 70 or 80% ethanol. Comparison of the results for these two solvents showed that 80% ethanol was more suitable.</description><subject>ACEITUNA</subject><subject>ACIDE GRAS</subject><subject>ACIDOS GRASOS</subject><subject>BYPRODUCTS</subject><subject>Deacidification</subject><subject>ETANOL</subject><subject>ETHANOL</subject><subject>FATTY ACIDS</subject><subject>liquid‐liquid extraction</subject><subject>OILSEED CAKES</subject><subject>OLIVE</subject><subject>OLIVE CAKE</subject><subject>OLIVES</subject><subject>PROCESAMIENTO</subject><subject>PROCESSING</subject><subject>refining</subject><subject>SOUS PRODUIT</subject><subject>SUBPRODUCTOS</subject><subject>sulfur olive oil</subject><subject>TORTAS OLEAGINOSAS</subject><subject>TOURTEAU D'OLEAGINEUX</subject><subject>TRAITEMENT</subject><subject>TURKEY</subject><subject>TURQUIA</subject><subject>TURQUIE</subject><issn>0003-021X</issn><issn>1558-9331</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1991</creationdate><recordtype>article</recordtype><recordid>eNp9kD1PwzAYhC0EEqWwMDJ5RnJ5HSfGHkuhUKmoQ6nEFjn-aI1cDHFC6b8nKCA2ptNJz3PDIXROYUQBrq9uppBxDoXMD9CAFoUgkjF6iAYAwAhk9PkYnaT00lXBsmKAwq1V2hvvvFaNj684Opza4Noax-A_LI4-jPBsNsKPbWg8SY1aWxz8e-sN6QPbz6ZW-tfe-qRtCArvfLPBttnsA1ZBx00Mp-jIqZDs2U8O0Wp69zR5IPPF_WwynhOdQS4I45UWRuqqKkwhaJ4ZyUHpiuaOSdEhmaYGqKGOCZ7zjGprDZOaM-GYUZwN0WW_q-uYUm1d-Vb7rar3JYXy-6fy76cOhh7e-WD3_5DleDFZgqCiUy56xalYqnXtU7laSsoLKoF9AXvSccU</recordid><startdate>199111</startdate><enddate>199111</enddate><creator>Turkay, S. 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(Technical University of Istanbul, Istanbul, Turkey)</creatorcontrib><creatorcontrib>Civelekoglu, H</creatorcontrib><collection>AGRIS</collection><collection>CrossRef</collection><jtitle>Journal of the American Oil Chemists' Society</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Turkay, S. (Technical University of Istanbul, Istanbul, Turkey)</au><au>Civelekoglu, H</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Deacidification of sulfur olive oil. II. Multi-stage liquid-liquid extraction of miscella with ethyl alcohol</atitle><jtitle>Journal of the American Oil Chemists' Society</jtitle><date>1991-11</date><risdate>1991</risdate><volume>68</volume><issue>11</issue><spage>818</spage><epage>821</epage><pages>818-821</pages><issn>0003-021X</issn><eissn>1558-9331</eissn><abstract>In this study, laboratory‐scale multi‐stage cross‐ and counter‐current extractions of sulfur olive oil miscella with 70 and 80% ethanol saturated with hexane were investigated. For cross‐current extraction, the extraction factor for free fatty acids was constant in each extraction stage. Therefore, the extraction factors determined in single‐stage extractions were used to calculate the extracted free fatty acid percentages for cross‐current and counter‐current multi‐stage extractions and results were in close agreement with the experimental data. It was possible to determine the amount of solvent and the number of stages required for counter‐current extraction to remove the desired amount of free fatty acids from a given sulfur olive oil with 70 or 80% ethanol. Comparison of the results for these two solvents showed that 80% ethanol was more suitable.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer-Verlag</pub><doi>10.1007/BF02660594</doi><tpages>4</tpages></addata></record> |
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subjects | ACEITUNA ACIDE GRAS ACIDOS GRASOS BYPRODUCTS Deacidification ETANOL ETHANOL FATTY ACIDS liquid‐liquid extraction OILSEED CAKES OLIVE OLIVE CAKE OLIVES PROCESAMIENTO PROCESSING refining SOUS PRODUIT SUBPRODUCTOS sulfur olive oil TORTAS OLEAGINOSAS TOURTEAU D'OLEAGINEUX TRAITEMENT TURKEY TURQUIA TURQUIE |
title | Deacidification of sulfur olive oil. II. Multi-stage liquid-liquid extraction of miscella with ethyl alcohol |
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