2009
DOI: 10.2174/2211334710902030230
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Recovery of Phenolic Antioxidants from Olive Mill Wastewater

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Cited by 62 publications
(25 citation statements)
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“…Membrane operations (Table 4) can be considered a valid approach for the selective removal of polyphenols from OMW. Many studies indicate that the future direction of the processes for the recovery of antioxidants from OMW is presumably towards the utilization of membranes in a sequential design [3]. Russo used several microfiltration (MF) and ultrafiltration (UF) membranes to concentrate the recovered polyphenols from vegetation waters (VW), using a final reverse osmosis (RO) consisting of a polymeric hydranautics membrane (composite polyamide).…”
Section: Membrane (Filtration)mentioning
confidence: 99%
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“…Membrane operations (Table 4) can be considered a valid approach for the selective removal of polyphenols from OMW. Many studies indicate that the future direction of the processes for the recovery of antioxidants from OMW is presumably towards the utilization of membranes in a sequential design [3]. Russo used several microfiltration (MF) and ultrafiltration (UF) membranes to concentrate the recovered polyphenols from vegetation waters (VW), using a final reverse osmosis (RO) consisting of a polymeric hydranautics membrane (composite polyamide).…”
Section: Membrane (Filtration)mentioning
confidence: 99%
“…This waste stream is generated in several forms and compositions following the particular characteristics of the used extraction equipment, olive variety, season and maturity of the fruit [2]. Pressure and three phase centrifugation systems produce considerably more liquid effluent than two phase centrifugation process [3]. The discontinuous process produces less but more concentrated wastewater (0.5-1 m 3 per 1,000 kg) than the centrifugation process (1-1.5 m 3 per 1,000 kg) [4].…”
Section: Introductionmentioning
confidence: 99%
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“…The traditional three-phase systems for olive pressing produce three streams of olive oil, olive cake, and aqueous olive mill wastewater (OMW) while the two-phase systems separate the olive paste into two phases of olive oil and semisolid waste known as pomace. [1][2][3] While two-phase systems provide comparatively low OMW volumes but relevant quantity of organic matter, three-phase extraction systems, which involve the addition of water (up to 50 L/100 kg olive paste), give rise to an annual worldwide production of large amounts of OMW. 1 Since OMW has broad spectrum toxicity and antimicrobial activity, leading to a difficult biological degradation, its disposal is a major problem that needs to be addressed for the development of a sustainable olive oil industry.…”
Section: Introductionmentioning
confidence: 99%
“…The most abundant and interesting phenolic compounds present in OOWW from the two-phase olive oil system are hydroxytyrosol and tyrosol (Takaç and Karakaya, 2009). One of the explanations for the formation of hydroxytyrosol is the hydrolysis of oleuropein (the main biophenol in many olive varieties) due to the action of esterases and acid hydrolysis of secoiridoid derivatives caused by the addition of HCl to the OOWW during oil extraction.…”
Section: Introductionmentioning
confidence: 99%