Abstract

In oil-mills, olive-pomace recentrifugation is a common way to reduce pomace moisture and, at the same time, to recover the oil therein. According to current rules, the obtained oil is defined as “crude olive-pomace oil.” The aim of this work is to verify the effect of recentrifugation on specific chemical and molecular parameters of the crude olive-pomace oil, by comparing it with the corresponding virgin olive oil obtained from the same olive lots. In particular, the following were considered: (i) the polar compounds of the oils that include compounds originated from oxidative and hydrolytic degradation, analyzed by high-performance size exclusion chromatography (HPSEC), and (ii) the profile of DNA microsatellite molecular markers that was analyzed by using the High Resolution Melting (HRM) technique. The obtained results evidenced the significantly higher hydrolytic degradation of crude olive-pomace oil, compared with the corresponding virgin olive oil, but at an extent unlikely able to allow the detection of fraudulent admixtures with virgin olive oils. In addition, the findings demonstrated the feasibility of the application of the HRM analysis of DNA microsatellites to crude olive-pomace oil, able to reveal the alteration of the declared varietal profile of a virgin olive oil sample by simply checking the HRM curve profiles.

Highlights

  • The processing technology of olive oil extraction has changed considerably during time

  • The polar compounds (PCs) are constituted by the main classes of substances of oxidation (TAGPs and oxidized triacylglycerols (ox-TAGs)) and hydrolysis (DAGs) of triacylglycerols, 25 20 a b

  • The extent of the oxidative and hydrolytic degradation of the investigated crude olive-pomace oils ascertained by highperformance size exclusion chromatography (HPSEC) analysis of PCs confirmed the results obtained in a previous research [7] by the conventional analyses foreseen by EC Reg. 2568/1991 [26] and subsequent modifications and integrations

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Summary

Introduction

The processing technology of olive oil extraction has changed considerably during time. The 3-phase decanter produces high amounts of waste water, characterized by high contaminant capacity, due to the addition of warm water to olive paste prior to processing [2]. Developed with the aim of solving this problem, the successive 3-phase WWA-decanters avoid this inconvenience but lose oil yield, while the insertion of a variable dynamic pressure cone, as in the VDP-decanters, able to work with less diluted olive pastes, submits the olivepomace to an additional dynamic pressure allowing more oil to be recovered [1]. The older 2-phase decanters, which separate olive oil from a mixture of olivepomace and waste water, effectively reduce the amounts of waste water without losing oil yield [2]

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