INTEGRATED PROCESS FOR THE ECO-SUSTAINABLE PRODUCTION OF HIGH QUALITY EXTRA VIRGIN OLIVE OIL AND MICRONIZED BY PRODUCTS

Abstract

The invention relates to an integrated process for the eco-sustainable production of extra virgin olive oil and solid by-products rich in polyphenols, according to the principles of the circular economy. The multifunctional process starts from Olea europaea L., and produces an extra virgin olive oil (EVO) with a high content of hydroxytyrosol and derivatives, and wherein the stoned and de-oiled olive pomace leaving the mill from a two-phase controlled process, is directly transformed into a powder product useful in the food and nutraceutical field, with a high content of antioxidant active principles.

Even the leaves and apical twigs resulting from the olive harvest are treated directly in the mill to obtain a standardized powder product in the content of oleuropein, the bitter active ingredient of the fruit, a cardioprotective molecule with an antioxidant character.

Claims

1. An integrated process for the eco-sustainable production of extra virgin olive oil and solid by-products rich in polyphenols, said process comprising: A) a section for defoliation, twig removal and washing of the olives entering the process, comprising a scan of said olives with an optical sensor, which determines the degree of ripeness. B) a section of extraction from said olives of extra virgin olive oil (EVO) by mechanical means according to the continuous two-phase method, which in turn includes two production lines in parallel: the first one operates on olives with stone by means of ordinary cold extraction, and the second one operating by pressing and machine pitting the olives at the same time, with the production, from said second line, of a residue consisting of a stoned de-oiled olive paste; C) a treatment section of said stoned de-oiled olive paste directly connected to the outlet of said second production line, comprising a freeze-drying operation of said stoned de-oiled olive paste, with production of a solid lyophilisate containing polyphenols and of water, which is recirculated to said section A) for defoliation and washing of the olives; and D) a section for the treatment of olive leaves and apical twigs resulting from said section A) of defoliation and washing of the olives, and possibly other leaves resulting from olive tree pruning, including a drying operation in the drying chamber, with the production of a dried leaf product containing oleuropein and of water, which is recirculated to said section A) for defoliation and washing of the olives.

2. The integrated process according claim 1, wherein said section A) of defoliation and washing of olives comprises the following operations: a) defoliation, twig removal and rock removal of the olives fed to the process; b) washing, rinsing and drying the olives resulting from the previous operation; c) scanning of the olives resulting from the previous operation by means of a multiparametric fluorescence optical sensor, to obtain a non-destructive measurement of the state of ripeness of the olives by determining their chlorophyll and polyphenol contents.

3. The integrated process according to claim 1, wherein said second production line, comprises the following operations: d) pressing the olives under vacuum or in a controlled atmosphere, by means of an integral pitting machine, with separation of the olive pulp from the stone; e) malaxation of olive pulp under vacuum or in a controlled atmosphere, and at a controlled temperature; f) extraction of EVO oil with a two-phase centrifugal decanter, resulting in oil output on one side and de-oiled stoned olive paste output on the other; g) direct passage of the extracted oil to a collection tank with filter; h) collection in a storage tank of EVO oil from stoned olives, in an air-conditioned environment and with the possible use of inert gas; i) possible mixing in predetermined percentages with EVO oil obtained from said first production line operating on olives with stone; and j) bottling under inert gas blanket the oil obtained from the previous operation h) or i).

4. The integrated process according to claim 3, wherein said EVO oil obtained from operation h) is cut in predetermined percentages with EVO oil obtained from said first production line operating on olives with stone.

5. The integrated process according claim 3, wherein said de-oiled stoned olive paste obtained from said operation f) is directly fed to the freeze-drying operation of the treatment section of the said de-oiled stoned olive paste.

6. The integrated process according to claim 1, wherein said treatment section C) of the de-oiled stoned olive paste also comprises, after said freeze-drying operation, a micronization operation of said solid lyophilisate, resulting in the production of a micronized product rich in polyphenols having antioxidant activity.

7. The integrated process according to claim 6, wherein said treatment section C) for treating the de-oiled stoned olive paste comprises also after said micronization operation, a packaging operation, followed by a final treatment in a sanitization tunnel with UV-C rays.

8. The integrated process according to claim 1, wherein said section D) for treating olive leaves and apical twigs also comprises, after said drying operation, a mixing operation of said dry leaf product, with production of a micronized rich in oleuropein with antioxidant activity.

9. The integrated process according to claim 8, wherein said section D) for treating olive leaves and apical twigs also comprises, after said micronization operation, a packaging operation, followed by a final treatment in a sanitization tunnel with UV-C rays.

10. The integrated process according to claim 3, wherein the EVO oil obtained from said bottling operation j) having a content of hydroxytyrosol and derivatives thereof higher than 250 mg/kg.

11. The integrated process according to claim 6, wherein the product obtained from said operation of micronization of the solid lyophilisate of de-oiled stoned olive paste has a content of hydroxytyrosol and derivatives higher than 1500 mg/kg.

12. The integrated process according to claim 8, wherein the micronized product obtained from said operation of micronization of said dry leaf product has an oleuropein content higher than 15% by weight.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0034] The specific features of the invention, as well as its advantages, will be more evident with reference to the attached figures, in which:

[0035] FIG. 1 shows a schematic and symbolic representation of the integrated process for the production of high-quality EVO oil and micronized byproducts rich in polyphenols according to the present invention, of products obtained therefrom and relative uses;

[0036] FIG. 2 is a schematic flow chart illustrating a specific embodiment of the integrated process according to the invention.

DETAILED DESCRIPTION OF THE INVENTION

[0037] Therefore, the specific object of the present invention is an integrated process for the eco-sustainable production of extra virgin olive oil and solid byproducts rich in polyphenols, comprising:

[0038] A) a section for defoliation, twig removal and washing of the olives entering the process, including a scan of said olives with an optical sensor, which determines the degree of ripeness.

[0039] B) a section of extraction of extra virgin olive oil (EVO) from said olives by mechanical means according to the continuous two-phase method, which in turn includes two production lines in parallel: the first one operates on olives with stone by means of ordinary cold extraction, and a second one operating by pressing and machine pitting the olives at the same time, with the production, from said second line, of a residue consisting of a stoned de-oiled olive paste;

[0040] C) a treatment section of said stoned de-oiled olive paste directly connected to the outlet of said second production line, comprising a freeze-drying operation of said stoned de-oiled olive paste, with production of a solid lyophilisate containing polyphenols and of water, which is recirculated to said section A) for defoliation and washing of the olives; and

[0041] D) a section for the treatment of olive leaves and apical twigs resulting from said section A) of defoliation and washing of the olives, and any other leaves resulting from olive tree pruning, including a drying operation in the drying chamber, with the production of a dried, containing oleuropein leaf product and of water, which is recirculated to said section A) for defoliation and washing of the olives.

[0042] The salient features of the integrated process proposed for the production of high-quality EVO oil and for the immediate recovery of its by-products rich in polyphenols, according to the present invention, are summarized schematically in the attached FIG. 1, together with the indication of the products obtained from it and the sectors in which these products find their place.

[0043] Preferably, the aforementioned EVO oil extraction section includes the following preliminary operations: [0044] a. defoliation, twig removal and stone removal of the olives fed to the process; [0045] b. washing, rinsing and drying the olives resulting from the previous operation; [0046] c. scanning of the olives resulting from the previous operation with a multiparametric fluorescence optical sensor, for the non-destructive measurement of the state of ripeness of the olives by determining their chlorophyll and polyphenol content.

[0047] As already noted, an instrument that meets these requirements is the Multiplex (Force-A), which in its original version is a portable fluorescence optical sensor, powered by batteries and normally usable in field, directly on the plant. The sensor comprises four LED excitation sources with spectral bands in UV-A (375 nm), blue (460 nm), green (515 nm) and red (637 nm) and three channels of photodiode detectors in the blue spectral regionsgreen, red and near infrared. The choice of sensor excitation sources is linked to the absorption wavelengths of the main substances of interest, such as anthocyanosides (520 nm), pigments of red or olive varieties, flavonols (350 nm). The excitation source at 375 nm, in fact, overlaps with the absorption of luteolin and apigenin, flavones or yellow pigments with an antioxidant character of the fruit, while the sources in blue and green overlap with the absorption of anthocyanosides.

[0048] According to the invention, the possible use of the instrument or of specific LEDs is also envisaged also inside the aforementioned leaf drying chamber, in order to be able to acquire specific data of functional quality and presence of active ingredients in the leaves to evaluate, during the drying phase, the content in total chlorophylls, total flavonoids and secoiridoic derivatives containing ortho-phenols. Therefore, acquisitions of chlorophyll index, flavonoid index and simple phenol index are foreseen, both on the raw material and on the post-drying products and on the post-treatment freeze-drying products obtained from said stoned de-oiled olive paste.

[0049] The additional features of the integrated process for the eco-sustainable production of high-quality EVO oil and micronized by-products rich in polyphenols according to the invention are defined in subsequent claims 3-12.

Example

[0050] A specific embodiment of the integrated process according to the present invention is described in the following by way of mere example but not limiting, together with the results of the experiments carried out on the products obtained therefrom. The same embodiment is illustrated in the block diagram presented in FIG. 2.

[0051] Production of Organic Olives and Biodynamic Olives Also Through the Use of Green Agriculture Formulas from Circular Economy

[0052] Field treatment is envisaged with green agricultural products admitted in the biological and biodynamic synergistic treatment, products that can also be obtained from the extracts and micronized products that can be obtained from the process phases described below. These products can be mixed with natural antimicrobials, in particular with compounds belonging to the class of hydrolysable tannins, or with natural condensates or volatile aromatic molecules obtained from extraction processes in a current of steam, such as hydro-essences and essential oils.

Features of Oil Mill

[0053] Defoliation, Reception of the Olives and Aspiration of the Leaves

[0054] The defoliation, twig removal, stone removal operation is carried out with an industrial defoliator, for example a floating compressed air industrial defoliator (Mercury).

[0055] Washing, Rinsing, Drying

[0056] Subsequently, the olives are washed with water in a recirculating washing machine for soft washing with the hydro bubble method, rinsed with disposable clean water, and dried with air blades.

[0057] According to the process of the invention, the water used for the washing phase of the olives is at least in part recovered from the subsequent phases of dehydration of the leaves and freeze-drying (lyophilization) of the stoned and de-oiled olive pulp obtained from the wet pomace.

[0058] Non-Destructive Monitoring of the State of Ripeness and of the Content of Polyphenols and Minor Polar Compounds in the Olives to be Subjected to Pressing.

[0059] According to the invention, the non-destructive monitoring of the ripening state of the olives and their content in polyphenols and minor polar compounds is envisaged using the Multiplex optical sensor as described above.

[0060] By placing the fluorometer in a fixed position on the inclined plane of the pressing to monitor the incoming olives, and connecting it with a computerized data acquisition and processing system, it is possible to create a database, customized by olive cultivar, relating to the content in red pigments, yellow pigments, secoiridoids (with particular reference to the oleuropein content) and chlorophyll of the treated olives. These parameters allow to have objective information on the degree of ripeness of the fruit and on the specific content of minor active compounds.

[0061] Downstream of the scanning with the Multiplex, olives enter one of two parallel extraction lines, which can be processed alternately or simultaneously, and one of which treat olives with stone (traditional pressing) and the other stoned olives.

[0062] Pressing

[0063] The pressing (continuous two-phase system) can be carried out in parallel with one of the following two methods:

[0064] a. Traditional cold pressing with crusher (Mori-TEM) with speed control and variable speed and control of the heat exchange, between the shell and the base, by means of water conveyed by a thermal generator, which allows to heat or cool if necessary.

[0065] b. Mechanical crushing carried out by means of an integral pitting machine (Mori-TEM), with the possible use of thermal control as required for traditional pressing (a) by making a bypass.

[0066] The olive paste obtained from each of the two pressings, in one case with ground pits and without pits in the other, then passes to the malaxation phase.

[0067] Malaxation

[0068] Each of the malaxators, which in the specific case are four in number, deals exclusively with one of the two olive pastes. It should be noted that each malaxator can be used for another batch of olive paste only after careful (automatic) washing of the machine with disposable water. Each malaxator is equipped with a vacuum pump, which can be equipped with gas generators (nitrogen, CO.sub.2 and ozone).

[0069] All the malaxators have safety valves and are equipped with specific software for monitoring the whole process, thanks to which it is possible to optimize customized process methods according to the cultivar and/or the degree of ripeness of the fruit, starting from a data collection database of previous productions. All this turns out to be extremely useful for the continuous process.

[0070] The system is also enhanced by the possible remote management through the additional use of cameras.

[0071] Separation of EVO Oil without the Need for a Vertical Centrifuge

[0072] For each of the two production lines of the crusher, a decanter of 1200 kg/h is used with a capacity between 900-1000 kg/h without adding water, with the possibility of managing the speed of revolutions between the auger and the drum in an interconnected way through the use of a pulley.

[0073] This allows to obtain EVO oil with different extractive characteristics, and therefore with different content in minor polar antioxidant compounds, as well as different presence of pectin in the olive paste. The latter, which for example, in the phase of high maturation of the raw material, absorb oil.

[0074] Collection and Filtration

[0075] For each of the two extraction lines there is a direct passage from the decanter to the collection tank with filter sheets (with different granulometry), connected to a pump with inverter which regulates the flow rate of the filter.

[0076] In this phase it is possible to use on-line control sensors at the output, such as a turbidimeter that allows the selection of the most suitable filter to exclude the risk of sedimentation.

[0077] Pre-Bottling Collection and Storage Tanks

[0078] The oil from traditional pressing and the oil from stoned olives are then sent to different tanks positioned in an air-conditioned environment and equipped with an internal temperature control sensor, and with the use of inert gas (e.g. argon) for optimal conservation of quality characteristics of the oil.

[0079] EVO Oil Bottling Line

[0080] Bottling takes place after any cutting between the two types of oil, in order to optimally calibrate the organoleptic characteristics, structure and shelf life of the resulting blend.

[0081] The bottling line is equipped with an inert gas system, preferably argon, to keep the quality of the oil unchanged for as long as possible.

Recovery of the Stoned Wet Virgin Pomace from a Two-Phase Process

[0082] Spray Freeze-Drying to Obtain Active Powders from Stoned De-Oiled Olive Pulp

[0083] The integrated process according to the invention provides for the sending of virgin pomace obtained from stoned olives directly to a freeze-drying (lyophilizing) spray system, for the production of active powders also functional as stoned de-oiled olive pulp.

[0084] Out of the decanter, the stoned de-oiled olive pulp is pumped into a system where the presence of liquid nitrogen, or of a refrigerator-reference group, allows the pasta to be frozen, which when nebulized, vacuum-packed, undergoes a fast process of dehydration in soft conditions for the maintenance of the content in active compounds, with particular reference to hydroxytyrosol, a primary molecule for the antioxidant characteristics in products and for the protection of human health.

[0085] Cold vacuum freeze-drying with a capacity of 200 kg/hour of product at 75% of water. The product obtained will have a water content <1% with a maximum treatment temperature of 30 C.

[0086] The plant consists of: [0087] a) Instant product cooler [0088] b) Microwave vacuum freeze dryer

a) Instant Cooler for Frozen Liquid Product

[0089] The product to be treated is pumped at high pressure into a heat exchange chamber where a rotating nebulizer nebulizes it in drops having sizes of the order of 200 microns.

[0090] The machinery consists of: [0091] 1000 litre storage tank complete with mixer used to homogenize the product; [0092] high pressure pump with a capacity of 400 litres/hour, maximum pressure 16 bar; [0093] spray chamber made of stainless steel, entirely coated with a thickness of 100 mm in high-density polyurethane foam; [0094] air flow separation cycle of ice particles, equipped with a guillotine valve used for unloading onto the conveyor screw; [0095] rotating nebulizer at 15000 rpm; [0096] producer of cold air at 10 C. with air-cooled refrigeration unit, thermal power 100 kW; [0097] blower with a maximum flow rate of 5000 cubic meters/hour controlled by an inverter; [0098] heat exchanger; [0099] electrical command and control panel.

[0100] Liquid nitrogen can be used instead of the cooling system by means of a refrigeration unit.

b) Continuous Vacuum Freeze Dryer

[0101] The machine, with a capacity of 200 kg/h of product to be treated, is made up of: [0102] tube heat exchanger equipped with product feed screw, [0103] star valve located at the outlet of the exchanger used to guarantee the maintenance of the vacuum;

[0104] vacuum intake tube;

[0105] condenser used to condense vapours, complete with sprayers to inject the product and prevent the exchanger tubes from freezing; [0106] liquid ring vacuum pump; [0107] refrigeration compressor with thermal 100 kW at 10 C., [0108] electrical operational and control panel.

[0109] The condensation water is 150 kg/hour with a natural composition from olive, and is reusable both in the washing processes of the raw material and in fertigation.

Olive Leaf Treatment Line

[0110] The leaf collection system provides, as described, the defoliation operation carried out in the mill, before pressing, and the presence of a basket for collecting the leaves within the crushing area itself or in a neighboring covered area.

[0111] Drying of the Olive Leaves in a Controlled Drying Chamber

[0112] This phase of the process involves the drying of olive leaves, harvested at different balsamic times. The operation has a high added value due to the presence of antioxidant components, with particular reference to oleuropein.

[0113] Below are the specifications of the drying chamber according to a preferred embodiment of the invention.

[0114] 1) Monitoring of the active ingredients of the fresh raw material, as input data.

[0115] 2) Customization of the laying of the material to be dried in controlled and monitored thicknesses in trays/baskets of free material, equipped with sensors for thermal control, humidity and movement, if necessary, of the container itself, all housed in mobile pallets.

[0116] 3) Dehydration in a controlled room equipped with a humidity extractor at controlled speed and suction capacity, presence of insulated walls with high prevalence flat fans and equipped with computer-controlled inverters for the control of flows and air circulation. Presence of both directional and diffusion sanitizing UV LEDs, of UV sanitizing and IR heating lamps (if necessary), and of controlled inputs for gases such as nitrogen, ozone, carbon dioxide and argon to be customized for modification and control of the process atmosphere. The chamber is equipped with temperature, humidity and gas composition control sensors.

[0117] 4) Equipped with nitrogen generator and ozone generator and housing of argon and carbon dioxide cylinders. All gases can be used both in the controlled drying and sanitization phases and as conditioning and sanitization of the environment and of the pipes, with management phases controlled by dedicated software, with personalization and storage of parameters and ramps as well of temperature, gas flows and humidity suction associated with activations with individual ramps and times of use of LEDs and UV lamps.

[0118] 5) Interior of the chamber in fully reflective food-compatible material and, depending on the required dimensions, the chamber itself can be equipped with an internal partition between the pallets, of minimum thickness, made of reflective material equipped with UV light LEDs widespread.

[0119] 6) Supply of condensate recovery container for food use, as a collection of micellar water, free from salts, usable both in the cosmetic sector and as a raw material in the design and manufacture of products for sanitization, including industrial.

[0120] 7) The chamber can be mobile or semi-mobile by means of use of a bed using a thickness of 15 cm from the ground or mobile trolley on wheels.

[0121] 8) Possible extra equipment of offline systems, control of product humidity and residual water activity in order to ensure the legal parameters of drying or dehydration required for each vegetable matrix.

[0122] The leaves can then be micronized as described below, for the production of standardized powders in oleuropein content.

[0123] Micronization to Obtain Active Powders from Olive Leaf and Dehydrated Olive Pulp

[0124] Both for the stoned de-oiled and freeze-dried olive pulp and for the dried leaves as described above, reduction into a fine powder is envisaged by means of a mechanical blade and/or mechanical ball micronizer. The micronizer is made of steel for food use, and allows to obtain powders with differentiated grain size, with temperature and humidity control and, according to the equipment of other areas of the plant, it has the possibility of mechanical control and of inertizable blanket.

[0125] Active Powder Packaging Line

[0126] The process of the invention provides for a post-micronization packaging system in the absence of air and sanitization, according to regulations, of the packaged product by means of a tunnel with UV-C LEDs.

[0127] In particular, both for the micronized from olive leaves previously sanitized in the drying chamber, and for the micronized products obtained by freeze-drying stoned de-oiled olive pulp, it is envisaged to be packaged in polymeric bags permeable to UV-C radiation with controlled thickness, in order to correctly eliminate internal oxygen and allow the permeation of sanitizing radiations on at least 95% of the surface of the packaged powders.

[0128] The designed sanitizing tunnel is also designed for packaging in an inert atmosphere, and provides for irradiation of the entire packaging surface, with the presence of a UV-C irradiation time control sensor.

Alternative Treatment of Dried Olive Leaves

[0129] Dynamic Solid-Liquid Extraction of Dried Leaves

[0130] As an alternative to micronization for the marketing of olive leaf powder in solid form, to be used for example for antioxidant herbal teas with a high oleuropein content, the leaves thus dried can also be subjected to dynamic liquid-solid extraction, in order to obtain standardized liquid solutions in oleuropein content.

[0131] The dynamic liquid-solid extraction is governed by the principle according to which the generation, with a suitable solvent, of a negative pressure gradient between the inside and the outside of a solid that contains extractable material, followed by a sudden restoration of the conditions of initial equilibrium, induces the forced extraction of the compounds not chemically bound to the main structure of which the solid is constituted. On the basis of this principle, pressure and depression cycles are applied to the extracting liquid which is in contact with the vegetable solid matrix, from which the active ingredients are extracted with extreme efficiency (Naviglio Extractor).

[0132] From the described operation, a liquid extract rich in oleuropein and a solid residue are obtained which can be used for field spreading as a bio-fertilizer.

Treatment of Wet Virgin Pomace with Ground Pits from a Two-Phase Process

[0133] The portion of wet pomace coming from the traditional extraction line, which contains ground pits, can be subjected to separation to recover the ground pits.

[0134] Separation of the Ground Pits for Energy Purposes and Cosmetic Uses

[0135] In addition to the use of the ground pits for energy purposes, it is possible to treat the latter in a micronizer in order to obtain powders that can be used both in cosmetics, such as powders for scrubs, and for the formulation of green agricultural products.

[0136] Finally, the fraction of wet pomace that remains from the separation of the ground pits can be delivered for the production of biogas, or used for field spreading, or even be sent to pomace oil extraction.

Study of the EVO Oil Produced

[0137] Two different types of EVO oil, produced according to the technologies of the present invention and referred to here as Sample A and Sample B, have been subjected to analysis to verify their quality in terms of controlled acidity, low number of peroxides and content in polyphenolic compounds complying with the indications of EFSA (EU No. 432/2012).

[0138] The qualitative-quantitative analysis with HPLC-DAD-MS (high performance liquid chromatography coupled with a diode array detector and mass spectrometry) was carried out at three control points: [0139] 1. at bottling; [0140] 2. after 6 months from bottling; [0141] 3. after 18 months from bottling.

1. Control Point at Bottling

[0142]

TABLE-US-00001 Sample A Sample B Compounds mg/L mg/L Hydroxytyrosol 9.73 10.26 Tyrosol 7.98 6.97 Elenolic acid derivatives 9.28 7.13 Elenolic acid 55.06 44.62 10-hydroxyoleocanthal 149.7 209.49 Oleocanthal 164.5 143.57 Summation of secoiridoid 171.01 153.25 derivatives Lignans 85.91 79.73 Oleuropein aglycone 170.37 141.24 Total minor polar com- 823.53 796.26 pounds (MPCs) MPC excluding elenolic 759.2 744.51 acid and derivatives Determination of the number of active meq O.sub.2 peroxides/kg Sample A 11.34 Sample B 11.84 Analysis of free acidity expressed as oleic acid (%) Sample A 0.09 Sample B 0.11 Determination of the number of polyphenols (mg/kg Tyrosol) Sample A 769 Sample B 879
2. Control Point after 6 Months

TABLE-US-00002 Sample A Sample B Compounds mg/L mg/L Hydroxytyrosol 18.43 16.46 Tyrosol 12.61 10.07 Elenolic acid derivatives 7.73 9.14 Elenolic acid 66.86 59.73 10-hydroxyoleocanthal 119.22 211.47 Oleocanthal 126.42 118.55 Summation of secoiridoid 158.06 87.28 derivatives Lignans 69.91 65.44 Oleuropein aglycone 171.30 137.08 Total minor polar com- 750.53 715.23 pounds (MPCs) MPC excluding elenolic 675.95 646.36 acid and derivatives Determination of the number of active meq O.sub.2 peroxides/kg Sample A 11.2 Sample B 12.5 Analysis of free acidity expressed as oleic acid (%) Sample A 0.29 Sample B 0.42 Determination of the number of polyphenols (mg/kg Tyrosol) Sample A 517 Sample B 574
3. Control Point after 18 Monthsi

TABLE-US-00003 Sample A Sample B Compounds mg/L mg/L Hydroxytyrosol 0.41 0.78 Tyrosol 0.06 0.38 Elenolic acid derivatives 11.39 13.23 Elenolic acid 65.01 62.41 10-hydroxyoleocanthal 70.56 84.28 Oleocantale 68.68 76.55 Summation of secoiridoid 33.41 35.71 derivatives Lignans 24.56 28.27 Oleuropein aglycone 98.22 83.01 Total minor polar com- 372.31 384.62 pounds (MPCs) MPC excluding elenolic 295.91 308.98 acid and derivatives Determination of the number of active meq O.sub.2 peroxides/kg Sample A 12.97 Sample B 11.17 Analysis of free acidity expressed as oleic acid (%) Sample A 0.72 Sample B 0.59 Determination of the number of polyphenols(mg/kg Tyrosol) Sample A 376 Sample B 394

[0143] The limits imposed in order to consider EVO oil as eligible for a health claim according to EU Regulation No. 432/2012 are, as is known, 5 mg of hydroxytyrosol and its derivatives per 20 g of oil. In total, therefore, 250 mg of hydroxytyrosol and derivatives per kg of EVO oil.

[0144] The total of compounds whose content in the oil must be counted for this purpose is the sum of the active molecules such as Sample C.

[0145] As can be seen, the two samples A and B given as an example largely comply with the request to allow an intake of at least 5 mg of hydroxytyrosol and derivatives in 20 of oil, necessary to be able to consider them beneficial for cardiovascular prevention.

[0146] In addition, the results obtained from the characterization of two other samples of EVO oil obtained by implementing the integrated process of this invention and the related considerations for compliance with the requirements of EFSA are reported. The samples are referred to here as Sample C and Sample D.

[0147] HPLC-DAD-MS Characterization Analysis of the Two EVO Oils Sample C and Sample D

TABLE-US-00004 Sample C Sample D Compounds mg/L mg/L Hydroxytyrosol 9.29 7.90 Tyrosol 6.23 6.13 Elenolic acid derivatives 36.90 30.40 Elenolic acid 80.42 70.74 10- hydroxyoleocanthal 193.17 162.82 oleocantale 31.22 49.53 Summation of secoiridoid 34.35 23.39 derivatives Lignans 152.24 166.05 Oleuropein aglycone 112.99 121.01 MPC excluding elenolic 656.81 637.96 acid and derivatives MPC excluding elenolic 539.48 536.82 acid and derivatives

Analysis of Free Acidity Expressed as Oleic Acid (%)

[0148]

TABLE-US-00005 Sample C 0.21 Sample D 0.16

Determination of the Number of Active Meq O.SUB.2 .Peroxides/Kg

[0149]

TABLE-US-00006 Sample C 7.79 Sample D 6.98

[0150] Considering also in this case the compounds that contribute to the count of beneficial active ingredients according to EFSA, namely hydroxytyrosol, tyrosol, 10-hydroxyoleocanthal and oleuropein aglycone, it appears that for the EVO oil of Sample C the contents of these compounds correspond to a total of 315.45 mg/L, equal to 342.88 ppm, which correspond to 6.8 mg compared to the 5 mg required.

[0151] For EVO oil Sample D, the levels of these compounds correspond to a total of 291.76 mg/L, equal to 317.13 ppm, corresponding to 6.3 mg compared to the 5 mg required.

Study of the Functional Quality of Olive Leaves and Stoned De-Oiled Olive Paste.

[0152] Production of Standardized Micronized Products in Oleuropein from Olive Leaves

TABLE-US-00007 Micronized olive Micronized olive leaves cv leaves cv Seggianese Seggianese in pruning in pressing Compounds (mg/g) (mg/g) Hydroxytyrosol glucoside 1.62 0.11 1.31 0.05 Hydroxytyrosol 1.02 0.04 Nd Elenolic acid diglucoside 10.33 0.61 9.26 0.41 Derivative caffeic acid 2.21 0.09 Nd Verbascoside 5.28 0.24 3.01 0.12 Luteolin 7-O-glucoside 3.60 0.14 1.83 0.07 Oleuropein 217.4 15.8 110.16 9.13 Oleuropein aglycone 27.84 1.13 2.51 0.10 Total polyphenols 269.30 18.16 128.08 9.88
Production of Standardized Micronized Products in Hydroxytyrosol from Olive Pulp

TABLE-US-00008 Olive pulp de- oiled and dried Compounds Olive pulp (mg/kg) (mg/kg) Hydroxytyrosol 6917.0 269 1266.4 48.1 Tyrosol 3744.1 146 415.9 15.8 Verbascoside .sup.5830 227 183.6 7.16 Total polyphenols 16491.1 642 1865.9 71.06

[0153] As previously described in relation to the use of Multiplex technology, the micronized from olive leaf and stoned and de-oiled olive pulp were also characterized using this instrumentation. In particular, it was possible to evaluate the content in total chlorophylls, total flavonoids and secoiridoid derivatives containing ortho-phenols, in order to obtain innovative parameters with a non-destructive method to be included in the product data sheet.

[0154] Both the micronized from leaves and the stoned and de-oiled olive pulp, standardized in the content of active ingredients and fibres, can be used in the food, nutraceuticals, cosmetics, animal feed and green agriculture sectors. Their use as active ingredients, with particular regard to the food and nutraceutical sectors, allows the formulation of products that can guarantee the daily intake of portions or doses which, containing 1-5 grams of micronized olive pulp and from leaf as a single ingredient or in mixture, per kg of micronized product, they guarantee an intake of hydroxytyrosol and derivatives of 5 mg/day as prescribed in the EFSA health specifications indicated above.

[0155] The present invention has been described with reference to some of its specific embodiments, but it is to be understood that variations or modifications may be made to it by those skilled in the art without thereby departing from the scope defined by the claims.