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dc.creatorDali, Imen
dc.creatorAydi, Abdelkarim
dc.creatorStamenić, Marko
dc.creatorKolsi, Lioua
dc.creatorGhachem, Kaouther
dc.creatorZizovic, Irena
dc.creatorManef, Abderrabba
dc.creatorDelgado, Daniel R.
dc.date.accessioned2022-03-04T11:27:30Z
dc.date.available2022-03-04T11:27:30Z
dc.date.issued2022
dc.identifier.issn1110-0168
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/4977
dc.description.abstractThe olive growing in Tunisia has an economic dominance and agricultural importance. However, the huge extraction of olive oil generates a large quantity of olive mill wastewater (OMW), which is discharged to the surroundings. The highly polluting potential (organic load) of OMW threatens the environment and requires an urgent solution. Supercritical fluid extraction (SFE) is a green extraction method that can be applied to purify OMW and, at the same time, to isolate a high quality oil from this wastewater. In order to explore and to valorize the compositions of Olive mill wastewater (OMW), extraction in different solvents (supercritical CO2, hexane) was carried out and chemical composition of the extracted oils were established by GC-FID. The Tunisia OMW were collected from two different zones namely Sousse and Sfax. In this work, we have investigated the effects pressure (P) and temperature (T) on the yield and the quality of oil. The suitable conditions for the extraction of oil from lyophilized OMW by Super-critical carbon dioxide (SC-CO2) were found to be the pressure of 30 MPa and the temperature of 60 degrees C. In order to simulate the process, the model of broken and intact cells (Sovova's model) was applied. The model well represented the experimental data.en
dc.rightsrestrictedAccess
dc.rights.urihttps://creativecommons.org/licenses/by-nc-nd/4.0/
dc.sourceAlexandria Engineering Journal
dc.subjectSupercritical CO2en
dc.subjectLipidsen
dc.subjectOlive mill wastewateren
dc.subjectModelingen
dc.subjectSovova's modelen
dc.titleExtraction of lyophilized olive mill wastewater using supercritical CO2 processesen
dc.typearticle
dc.rights.licenseBY-NC-ND
dc.citation.epage246
dc.citation.issue1
dc.citation.other61(1): 237-246
dc.citation.rankM21~
dc.citation.spage237
dc.citation.volume61
dc.identifier.doi10.1016/j.aej.2021.04.0881110-0168
dc.identifier.wos000709490700022
dc.type.versionpublishedVersion


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