METHOD FOR THE OPTIMISATION OF ORGANOLEPTIC PROPERTIES IN VEGETABLE PRODUCTS CONTAINING CHLOROPHYLLOUS PIGMENTS

Abstract

The present invention relates to a process enabling the optimisation of the organoleptic properties, particularly the colour, of vegetal products containing chlorophyll pigments, comprising a pheophytinisation treatment of the vegetal products, a treatment with a solution having a pH higher than 5, and a treatment with at least one divalent metal compound.

Claims

1. A process for the optimisation of the organoleptic properties of vegetal products containing chlorophyll pigments, comprising the following stages: pheophytinisation treatment of the vegetal products for the replacement of Mg by 2H in at least 10% of the chlorophyll compounds, wherein said treatment is a heat, biochemical or chemical treatment, wherein the chemical treatment does not comprise the use of a buffered acid solution; treatment of the vegetal products with a solution at a pH of between 5 and 12, to maintain the pH of the vegetal products at a value of over 5, and treatment of the vegetal products with at least one divalent metal compound selected from among Ca, Fe, Mn and Zn or combinations thereof, for the formation of divalent metal chlorophyllcomplexes.

2. The process for the optimisation of the organoleptic properties of vegetal products containing chlorophyll pigments, according to claim 1, characterised in that the organoleptic property to be optimised is the green colour.

3. The process according to claim 1, wherein the vegetal products are selected from among fruits and/or vegetables containing chlorophyll pigments, such as table olives, peas, artichokes, chard, capers, cabbage, spinach, garlic sprouts, cardoons, turnip tops, broad beans, green beans, green asparagus, green peppers, broccoli, gherkins, avocados, plums, kiwis, apples, pears and grapes.

4-5. (canceled)

6. The process according to claim 1, wherein the pheophytinisation treatment is performed during a period of between 3 years and 5 minutes, and prior to the treatment with the solution that maintains the pH of the vegetal products at a value above 5.

7. The process according to claim 1, wherein the vegetal products are maintained at a pH of between 5 and 8.

8. The process according to claim 1, wherein the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5 is performed prior to the treatment of the vegetal products with at least one divalent metal compound.

9. The process according to claim 1, wherein the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5 and the treatment of the vegetal products with at least one divalent metal compound are performed simultaneously.

10. The process according to claim 1, wherein the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5 is performed subsequent to the treatment of the vegetal products with at least one divalent metal compound.

11. The process according to claim 1, wherein the pheophytinisation treatment and the treatment of the vegetal products with at least one divalent metal compound are performed simultaneously.

12. The process according to claim 1, wherein the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5, the pheophytinisation treatment and the treatment of the vegetal products with at least one divalent metal compound are performed simultaneously.

13. The process according to claim 1, wherein the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5 is performed subsequent to the simultaneous performance of the pheophytinisation treatment and the treatment of the vegetal products with at least one divalent metal compound.

14. The process according to claim 1, wherein the pheophytinisation treatment is a heat treatment.

15-17. (canceled)

18. The process according to claim 1, wherein the pheophytinisation treatment is a biochemical process.

19-21. (canceled)

22. The process according to claim 1, wherein the pheophytinisation treatment is a chemical treatment.

23. The process according to claim 22, wherein the chemical treatment is a treatment with an acid solution.

24. (canceled)

25. The process according to claim 23, characterised in that the treatment with the acid solution consists of placing the vegetal products in contact with the solution at a concentration equal to or greater than 0.1 mM, during a period of time of between 1 minute and 2 years, at a temperature between 4 C. and 100 C.

26. The process according to claim 1, wherein the divalent metal compound is a zinc compound.

27-28. (canceled)

29. The process according to claim 1, characterised in that the solution at a pH of between 5 and 12, employed to maintain the pH of the vegetal products at a value above 5, is selected from among sodium, potassium, ammonium or magnesium hydroxide or carbonate, or combinations thereof, or a boric-borate, glycine-glycinate, phosphoric-phosphate, carbonic-carbonate buffered solution, or combinations thereof.

30-31. (canceled)

32. A vegetal product comprising a percentage of divalent metal chlorophyllcomplexes, with regard to the total quantity of chlorophyll compounds, of between 15% and 100%, the divalent metal being selected from among Ca, Fe, Mn and Zn, or combinations of the same.

33. The vegetal products according to claim 32, characterised in that the chlorophylldivalent metal complexes are Znchlorophyll complexes present in a percentage of between 15% and 100%, and in the Zn content of between 0.3% and 0.0005%.

34-36. (canceled)

37. The vegetal products according to claim 32, wherein the vegetal products employed for the application of the process are selected from between green table olives processed by means of alkaline treatment and with or without lactic acid fermentation, and green table olives processed au naturel, with or without lactic acid fermentation.

Description

DESCRIPTION OF THE DRAWINGS

[0066] FIG. 1: Effect of the treatment with zinc acetate at a pH of 5.5 on the greenness of the table olive, estimated from parameter a*. The Zn.sup.2+ ions are added at a concentration of 3 g/L (3000 ppm) in an acetic/acetate buffer solution at 0.1M, at a pH of 5.5 and containing 6% of NaCl (w/v). with Zn.sup.2+.box-tangle-solidup. control without Zn.sup.2+. Note: Accelerated storage test, consisting of subjecting the treated olives to a temperature of 55 C. during 24 hours.

[0067] FIG. 2: Typical reverse-phase HPLC chromatograms with detection at 640 nm, for the separation of chlorophylls, Mg-free chlorophyll derivatives and Zn metallochlorophyll complexes in green table olives of the Manzanilla variety, according to the different stages of the Castelvetrano-style preparation process (CSP) and the performance of the invention in accordance with example no. 1: (A) Fresh fruit; (B) CSP fruit, (C) CSP fruit treated subsequently with 3 g/L (3000 ppm) of Zn.sup.2+ ions dissolved in NaCl brine at 4% (w/v), buffered at a pH of 5.5 with 0.1M of acetic acid/acetate: (C1) for 14 days, (C2) for 6 months, (C.sub.3) for 10 days+accelerated storage test (24 h at 55 C.). Identification of peaks: Chlorophylls: 3. Chlorophyll b; 4. Chlorophyll a; Precursors of zinc metallochlorophyll complexes of the series a: 1. 15.sup.2 methyl-phytol-chlorine e.sub.6 ester; 9. Pheophytin a; 10. Pheophytin a; 11. Pyropheophytin a. Zinc metallochlorophyll complexes of the series a: 2. Zn-15.sup.2 methyl-phytol-chlorine es ester; 5. Zn-15.sup.1-OH-Lactone Pheophytin a; 6. Zn-Pheophytin a; 7. Zn-Pheophytin a; 8. Zn-Pyropheophytin a.

[0068] FIG. 3: Typical reverse-phase HPLC chromatograms with detection at 640 nm, for the separation of chlorophylls, Mg-free chlorophyll derivatives and Zn metallochlorophyll complexes in green table olives of the Manzanilla variety, according to the different stages of the Castelvetrano-style preparation process (CSP) and the performance of the invention: (A) Fresh fruit; (B) CSP fruit, (C) CSP fruit treated subsequent to 9 days' acid treatment in NaCl brine at 4% (w/v), buffered at a pH of 4 with 0.1M of lactic acid/NaOH (CSP+Ac) in accordance with examples 2, 3 and 4; (D) CSP+Ac fruit sterilised at 117 C. for 43 min. in a 4% NaCl solution (w/v) with 0.1M glycine/NaOH at a pH of 9.5, containing 0.1 g/L (100 ppm) of Zn.sup.2+ ions, in accordance with example 4.2.

[0069] FIG. 4: Effect of the application of the invention to fresh green beans on (A) the greenness of the product, estimated as from parameter a*, and (B) the percentage of chlorophyll derivatives with Mg, 2H and with Zn, in accordance with the embodiments in examples 9 and 10. (A and B)

DETAILED DESCRIPTION OF THE INVENTION

[0070] The present invention relates to processes for the improvement of the green colour in prepared fruits and vegetables, particularly in green beans and table olives, employing a divalent metal salt. Preferably, food-grade zinc is employed; the quantity of Zn (II) added to the product does not necessarily have to exceed 100% of the NRV per 100 g of product. The process may be applied to any product containing chlorophyll pigments (chlorophylls and/or chlorophyll derivatives).

[0071] The invention encompasses any stage of the preparation of the fruits and vegetables when in said preparation divalent metal salts, preferably zinc, are employed for the improvement of the colour, and the purpose thereof is to provide an improvement in the colour of the product by means of the formation of metallochlorophyll complexes of a divalent metal, preferably zinc (Zn-Cls) of a highly stable bright green colour. The process may comprise the following stages:

[0072] A) pheophytinisation treatment

[0073] B) treatment with at least one salt of a divalent metal, preferably zinc

[0074] C) treatment with a solution with a pH of between 5 and 12, to maintain the pH of the vegetal products at a value above 5

[0075] D) washing and drying

[0076] E) packaging

[0077] F) heat preservation treatment

[0078] Stages of cutting or shredding the vegetal products may also be included; likewise the extraction of oil or juice and the addition of aromas and/or other ingredients and food additives.

[0079] The process enables the increase to the maximum of the efficacy of the complexing process with the divalent metal, and therefore the re-greening of the vegetal product, in a process comprising two fundamental technical characteristics not performed to date: (a) bringing about the replacement of Mg by 2H in a significant part of the chlorophyll compounds (pheophytinisation) as an essential prior step for the subsequent reaction of complexing with the divalent metal, and (b) controlling the pH of the complexing reaction at a value greater than 5.

[0080] With these technical characteristics, the process achieves: (a) an optimal green colour in vegetal products such as tinned beans, employing a lower quantity of zinc, without it being necessary to exceed 100% of the NRV (100 ppm); (b) the avoidance of copper to achieve an optimal colour; (c) stabilisation of the green colour, even in vegetal products with a low chlorophyll pigment content, such as olives; (d) reducing the number and/or intensity of the heat treatments, reducing to the maximum the issues regarding texture and cooked taste; and (e) in one specific application, stabilising the green colour of the vegetal product prior to the heat preservation process, enabling its preservation by pasteurisation under acidic conditions, or even preservation without heat treatment due to the chemical characteristics of the product.

[0081] The performance of these stages may follow different sequences, as indicated above, it being possible to perform several of the stages simultaneously.

[0082] The re-greening of the product is attributed to the formation of divalent metal metallochlorophyll complexes. When zinc is used, the complexes formed are principally Zn-pheophytin a, Zn-pyropheophytin a and Zn-15.sup.2-Me-phytol-chlorine e.sub.6 ester.

[0083] In the present invention, the term chlorophyll pigment refers to a coloured compound with a chemical structure derived from chlorophyll; that is, formed by a substituted porphyrin ring, with an additional isocyclic ring, which may be open, and a trace of esterified or otherwise propionic acid with a terpenic chain known as phytol. The porphyrin ring is a tetrapyrrole, with four pyrrole rings linked to form a larger ring, which is the porphyrin. In the case of chlorophyll, a Mg.sup.2+ atom linked to the nitrogens of the pyrrole groups is to be found in the centre of the porphyrin, but this Mg.sup.2+ atom may be replaced by a divalent metal or by 2H.sup.+ to form other chemically stable pigments.

[0084] The term green table olive refers to a product prepared from healthy fruits of farmed olive varieties, harvested during their ripening cycle, prior to colouring, when they have reached their normal size, and subjected to treatments to eliminate their natural bitterness and preserved by natural fermentation or heat treatment, with or without preservatives, and packaged with covering liquid. Examples of green table olives are green olives treated in brine, untreated green olives au naturel, or olive specialities processed by means of alkaline treatment and unfermented, which have specific names and characteristics in the different producer countries: Campo Real in Spain, Castelvetrano in Italy, Picholine in France, and Californian-style green olives or greenripe olives in the United States.

[0085] In the present invention, the term pheophytinisation treatment (stage A) refers to any physical (e.g. heat), chemical or biotechnological process causing the replacement of Mg by 2H in at least 10% of the chlorophyll compounds of the vegetal matter. The pheophytinisation treatment is selected from among a physical heating process, a chemical process under acidic conditions, a biotechnological acid fermentation process, or combinations thereof.

[0086] The physical heat treatment is a blanching/boiling of the vegetal product during a certain period of time. In a preferred embodiment, the treatment would be a heating of the vegetal products at a temperature of between 50 and 100 C. during a period of time of between 1 and 90 min. In a more preferred embodiment, the treatment would be performed at 97 C. during 20 min.

[0087] The chemical process under acidic conditions involves placing the vegetal material in contact with a solution with a pH lower than 7 during a certain period of time, at a product:liquid ratio which, at least, enables the covering of the vegetal material, or by a continuous flow of the solution. In accordance with a preferred embodiment, the solution is hydrochloric acid at a pH of 1.8 and with a concentration equal to or greater than 0.1 mM. The treatment time is between 1 min. and 2 years, preferably 9 days, at a temperature between 4 C. and 100 C., preferably an ambient temperature of 253 C. In another preferred embodiment, the treatment time is 20 min. and the temperature is 97 C.

[0088] The biotechnological fermentation process is the preservation of the vegetal material during a period of time by means of lactic acid fermentation. In accordance with a preferred embodiment, the natural fermentation takes place in NaCl brine at an equilibrium concentration of 7%, during a period of time exceeding 3 months, until a lactic acidity of at least 1.5% and a pH value below 5 is reached.

[0089] In the present invention, the term treatment with a divalent metal salt, preferably zinc (stage B) refers to placing the vegetal material in contact with a solution containing a divalent metal compound, preferably a zinc salt, during a certain period of time, at a product:liquid ratio which, at least, enables the covering of the vegetal material, or by a continuous flow of the solution. The divalent metal salt is a food-grade salt, preferably the food additive zinc acetate (E-650) or zinc chloride, at a concentration between 0.005 g/L (5 ppm) and 3 g/L (3000 ppm), preferably that which enables the obtaining of a product providing 100% of the NRV of zinc per 100 g of product. The treatment time is between 5 min. and 1 year, and the temperature between 4 C. and 150 C. In a preferred embodiment with olives, the treatment is performed for 48 hours at 253 C. In other preferred embodiments with vegetables, the treatment is performed for 5 days at 60 C. and for 45 min. at 97 C.

[0090] In the present invention, the term treatment with a solution with a pH of between 5 and 12 (stage C) refers to placing the vegetal material in contact with a solution with a pH of between 5 and 12 during a certain period of time, to maintain the pH of the vegetal products at a value above 5, at a product:liquid ratio which, at least, enables the covering of the vegetal material, or by a continuous flow of the solution. In accordance with a preferred embodiment, the solution is sodium hydroxide, at a concentration 0.1M and a pH of 13. The treatment time is between 5 min. and 1 year, and the temperature between 4 C. and 150 C. In a preferred embodiment with olives, the treatment is performed during 48 h at 253 C. followed by 43 min. at 117 C. In other preferred embodiments with vegetables, the treatment is performed for 5 days at 60 C. and for 45 min. at 97 C.

[0091] In the present invention, the term washes (stage D) refers to successive treatments of the vegetal material with water during a period of time. In a preferred embodiment, this treatment is performed by immersion of the fruit in water during a period of time of between 3 and 24 hours, preferably 12h, and the number of washes is between 0 and 5, in accordance with the acidity and/or the concentration of divalent metal, preferably zinc, employed in a previous stage. In a preferred embodiment, 5 washes are performed, of 12 hours each.

[0092] In the present invention, the term packaging (stage E) refers to the process by which the vegetal product is packed in a container for its transport and sale, in brine, in a controlled atmosphere or vacuum-packed. In a preferred embodiment, the packaging is performed by immersing the vegetal product in NaCl brine at a concentration between 0.12 and 6% (w/v), preferably 4%. If in one of the preferred embodiments the concentration of the divalent metal salt in stage B is 100% of the NRV, the washing stage (stage D) and the addition of brine in the packaging (stage E) may be eliminated.

[0093] In the present invention, the term heat preservation treatment (stage F) refers to a heat treatment that guarantees the long-term safety of the product. In a preferred embodiment, the heat treatment is a commercial sterilisation at a temperature between 117 C. and 150 C., preferably at 117 C., during a period of 43 min. In another preferred embodiment, the heat treatment is a pasteurisation, at a temperature between 60 and 95 C. In more preferred embodiments, the pasteurisation is performed at 80 C. during 8 min. or at 90 C. during 15 min.

[0094] For the analysis of chlorophyll pigments in general, their extraction is performed with acetone saturated with MgCO.sub.3. Starting from a weighed sample of shredded material, successive extractions are performed until colourless extracts are obtained, and next, a transfer of components to diethyl ether is carried out, in accordance with the methodology described by Minguez-Mosquera, Gandul-Rojas, Gallardo-Guerrero and Jarn-Galn, Chlorophylls. In Methods of Analysis for Functional Foods and Nutraceuticals; Hurst, W. J., Ed.; CRC Press: Boca Raton, Fla., 2002; pp 159-218. The ether phase is filtered through an anhydrous Na2SO4 bed to completely remove the water, and it is evaporated to dryness in a rotary evaporator. The dry residue is stored at 20 C. in an atmosphere of nitrogen until used.

[0095] For the analysis of chlorophyll pigments in olives, and given their high lipid content, a specific extraction technique is required; this has been developed by Minguez-Mosquera and Garrido-Fernndez Chlorophyll and carotenoid presence in olive fruit, Olea europea. J. Agric. Food Chem. (1989) 37, 1-7). The technique is based on an extraction with N,N-Dimethylformamide (DMF), followed by a selective distribution of components between this DMF phase and hexane. The lipids and the diesterified xanthophylls and carotene fraction remain in the hexane phase, while the DMF phase retains the chlorophyll compounds and the free and monoesterified xanthophylls. This system yields a solution of pigments free of the fatty matter which is characteristic of these fruits and which interferes in the subsequent separation and identification of the pigments.

[0096] Once the pigment extract has been obtained, the separation and quantification of pigments is carried out by means of HPLC with a reverse phase column (200.46 cm) packed with Mediterranea-Sea C18 (3 m) (Teknokroma, Barcelona, Spain). The column is protected with a pre-column (10.4 cm) packed with the same material. The separation is performed at a flow rate of 1.25 mUmin., by means of a gradient elution employing two blends of solvents: A. Water/ion-suppressing reagent/methanol (1:1:8 v/v/v) and B.-methanol/acetone (1:1 v/v). The ion-suppressing reagent is tetrabutylammonium acetate 0.05 M and ammonium acetate 1M in water (Minguez-Mosquera, Gandul-Rojas, Montao-Asquerino and Garrido-Fernndez Determination of chlorophylls and carotenoids by HPLC during olive lactic fermentation. J. Chromatogr. (1991) 585, 259-266). The gradient system employed is an adaptation of that described by Gandul-Rojas, Roca and Gallardo-Guerrero Detection of the colour adulteration of green table olive with copper chlorophyllin complexes (E-141ii colorant). LWTFood Sci. Tech. (2012) 463, 11-318.

[0097] The spectrophotometric detection of the chlorophyll pigments is performed at 666, 650, 640 and 626 nm, and an on-line record of the UV-Vis absorption spectrum is obtained with a photodiode detector. The identification is performed by means of co-chromatography with the corresponding standards and from the spectral characteristics described in detail in specific publications (Minguez-Mosquera, Gandul-Rojas, Gallardo-Guerrero and Jarn-Galn Chlorophylls. In Methods of Analysis for Functional Foods and Nutraceuticals; Hurst, W. J., Ed.; CRC Press: Boca Raton, Fla., 2002; pp 159-218). The quantification is performed by means of the corresponding calibration curve (quantity vs integrated peak area). The calibration equations are obtained by linear regression analysis of least squares in a range of concentration in accordance with the levels of concentration of these pigments in table olives. Duplicate analyses of 5 different volumes of each standard solution are performed.

[0098] To determine the metal content, one commences with 100 g of fruit which are washed, dried, pitted and shredded. From the resulting paste, exactly 5 g is weighed into a porcelain capsule and is placed in a muffle furnace. The temperature of the muffle is raised rapidly to 100 C. and then is raised slowly until it reaches the calcination temperature (550 C.), at which it is maintained for 8-10 hours. The ashes, of a greyish-white colour, are moistened slightly and dissolved in three 2-mL portions of HCL 6 N and gradually filtered through filter paper into a 25-mL calibrated flask. Subsequently, the filter is washed three times with 3 mL of deionised water, which is also added to the calibrated flask; this is finally made up to volume with deionised water. The dissolving of the ashes is facilitated by heating the capsule slightly after each addition of HCl. In parallel, a blank is prepared which only contains the reagents. Finally, the metal content is determined with an atomic absorption spectrophotometer (GBC, model 932) equipped with two multi-element cathode lamps (Cu, Fe, and Mn) (GBC, Victoria, Australia) and (Ca, Mg, Cu and Zn) (Photometry, Victoria, Australia). The sample is nebulised in an air-acetylene flame and the instrumental conditions for the measurement of the absorbance are established in accordance with the equipment manual (Lpez-Lpez, Garca-Garca and Garrido-Fernndez Multivariate characterization of table olives according to their mineral nutrient composition. Food Chem. (2008) 106:369-378).

[0099] The measurement of the colour is obtained with a BYK-Gardner, Model 9000 spectrophotometer equipped with a software to calculate the chromatic coordinates in the CIELAB scale. The datum for each measurement will be the average value obtained with 20 samples of shredded olives or beans (Arroyo-Lpez, Romero, Durn-Quintana, Lpez-Lpez, Garca-Garca and Garrido-Fernndez Kinetic study of the physicochemical and microbiological changes in seasoned olives during the shelf-life period. J. Agric. Food Chem. (2005) 53, 5285-5292). The changes in the green colour are expressed with the L*, a*, b* parameters, the a*/b ratio, angle of hue (h) and chroma (C*) (Koca, Karadeniz, Burdurlu Effect of pH on chlorophyll degradation and colour loss in blanched green peas. Food Chem. (2006) 100, 609-615).

Embodiment of the Invention

[0100] The invention will be illustrated below by means of a number of assays performed, which highlight the efficacy of the process described in the present invention.

[0101] Raw Material for Examples 1 to 5.

[0102] A 78-kilo batch of olive fruits of the Manzanilla variety, collected mostly in the yellowish-green state of ripeness, was processed on a laboratory scale as green table olives treated with alkali and not fermented, in accordance with the Castelvetrano style. Before processing, a manual selection of the fruit was performed, eliminating those damaged or in different states of ripeness (mottled, purple or black). These selected fruits were placed in PET containers with a capacity of 3.7 L and were covered with a solution of NaOH at 2% (w/v) (2.2 kg of fruit+1.8 L of alkaline solution). After an hour of treatment, 100 g of NaCl was added to each container (equivalent to a final concentration of 5.5% in the NaCl/NaOH solution) and the fruits were maintained in this alkaline brine for 15 days, subsequently performing three washes with water, these lasting 3.5h, 18 h and 3.5h. Finally, the fruits were placed in NaCl brine at 6% (w/v) and were kept in a refrigeration unit at 4 C. until use.

Example No. 1: Pasteurised Product Prepared in Three Phases

[0103] In this example, the pheophytinisation treatment was performed by means of a chemical process under acid conditions and was performed simultaneously with the treatment of the vegetal products with the solution which maintains the pH of the vegetal products at a value above 5, and with the treatment of the vegetal products with at least one divalent metal compound.

[0104] Phase 1. Stages A, B and C: Pheophytinisation Treatment and Treatment with Zinc Salt in a Buffered Acid Solution.

[0105] Treatment of green table olives prepared in the Castelvetrano style in a 0.1 M solution of the acetic/acetate buffer mixture at a pH of 5.5, containing 6% (w/v) of NaCl and 3 g/L (3000 ppm) of Zn.sup.2+ ions as zinc acetate. The solid/liquid ratio is 1:3, and the treatment is 6 months at an ambient temperature of 253 C.

[0106] Glass jars with a capacity of 445 mL (16 Ref TO77) were filled with 20 olives (99-103 g) and 300 mL of the buffered brine containing 3 g/L (3000 ppm) of zinc acetate. The closed jars were kept in the laboratory at ambient temperature and in darkness, and were analysed with regard to colour and chlorophyll pigment content after 2, 4, 7, 8, 9, 10 and 14 days. Finally, the fruits were kept in store for 6 months, and alternatively were subjected to an accelerated storage test by heating in an oven at 55 C. during 24h. In parallel, checks were performed on fruits packaged and stored under identical conditions, but without the addition of Zn.sup.2+ to the packaging brine.

[0107] During storage, the loss of the green colour in the fruits, measured from the chromatic coordinate a*, was very slow in the fruits packaged with zinc, in no case being significant (p<0.05) (FIG. 1). Conversely, the fruits not treated with zinc underwent a much more rapid loss of greenness, starting to become significant as from day 9 (p<0.05). This loss of greenness was associated with the reaction of the replacement of the Mg.sup.2+ by 2H.sup.+ undergone by the chlorophylls and derivatives under acid conditions. Conversely, in the fruits treated with the Zn.sup.2+ salt, this reaction was counteracted by the insertion of this divalent metal into the porphyrin ring, bringing about the formation of metallochlorophyll complexes of a stable green colour. At day 8, the formation of these zinc metallochlorophyll complexes began to be apparent in the a series, slowly increasing their concentration until day 14 (FIG. 2 C.sub.1). By means of the accelerated storage test it was possible to bring about a highly significant re-greening of the fruit treated with zinc, the value of a* even surpassing the initial value (7.30) (table 1). This improvement in colour was associated with the formation of different zinc metallochlorophyll complexes, mainly of the a series (FIG. 2 C.sub.3). Quantitatively, the zinc metallochlorophyll complexes represent almost 45% of the total of chlorophyll pigments present in the olives subjected to the accelerated storage test (table 2).

TABLE-US-00002 TABLE 1 Chromatic coordinate a* in green table olives processed in accordance with different examples of the invention. Sample Stages of the invention.sup.1) a* FGO.sup.2) 12.52 0.01 CSPGO (i) 5.87 0.51 CSPGO (a) 2.68 0.42 A B C D E F Ex. 1.sup.3) BAS pH 5.5 with 3000 ppm of Zn (1:3) 5 YES P 7.30 0.51 BAS pH 5.5 (control without Zn) (1:3) 5 YES P 0.22 0.57 Ex. 2 BAS pH 4 BBS pH 9.5 + 5 YES P 1.53 0.25 (1:3) 3000 ppm of Zn (1:3) Ex. 3 BAS pH 4 BBS pH 9.5 (1:1) + 3.1 (1:3) 80 ppm of Zn 0.25 0.32 3.2 100 ppm of Zn NO YES P 0.30 0.27 3.3 120 ppm of Zn 0.35 0.41 3.4 140 ppm of Zn 0.33 0.28 3.5 Control without Zn 3.93 0.13 Ex. 4 BAS pH 4 BBS pH 9.5 (1:1) + 4.1 (1:3) 80 ppm of Zn 4.28 0.39 4.2 100 ppm of Zn NO NO S 4.61 0.58 4.3 120 ppm of Zn 4.71 0.71 4.4 140 ppm of Zn 5.00 0.39 Ex. 5 BAS pH 4 + 100 ppm (1:1) 5.1 of Zn (1:1) BBS pH 9.5 NO NO S 3.26 1.53 5.2 BBS pH 9 2.54 1.51 Ex. 6 AS pH < 2 BBS pH 9.5 + NO NO S 4.23 0.33 (4:3) 200 ppm of Zn (4:3) Ex. 7.sup.4) AS pH < 2 100 ppm of BS pH > 13 NO YES S 4.47 0.55 (4:3) Zn (4:3) Ex. 8 LAF pH < 4 BBS pH 9.5 + NO NO S 3.96 0.11 200 ppm of Zn (4:3)

TABLE-US-00003 TABLE 2 Percentage of chlorophyll pigments with Mg, with 2H and with Zn, and zinc content in green table olives processed in accordance with different examples of the invention, as described in table 1: Chlorophyll pigment (%) Zinc Sample with Mg with 2H.sup.+ with Zn.sup.2+ content (ppm) FGO.sup.2) 97.6 2.1 2.4 0.8 3.10 0.25 CSPGO (i) 50.1 4.4 49.9 4.4 Nd CSPGO (a) 29.7 15.5 70.3 15.5 Nd Ex. 1.sup.3) 20.5 1.1 34.6 0.1 44.9 1.2 Nd 18.5 0.5 81.5 0.5 Nd Ex. 2 0.4 0.3 22.0 2.0 74.4 1.4 503.2 34.2 Ex. 3 Nd Nd Nd Nd 3.1 3.2 3.3 3.4 3.5 Ex. 4 4.1 4.7 0.1 45.3 3.6 48.9 4.6 58.8 6.9 4.2 5.3 1.7 51.8 0.3 42.9 2.0 68.5 3.2 4.3 5.3 0.4 44.4 0.9 50.3 0.5 86.2 5.1 4.4 3.1 0.1 50.3 1.1 54.6 1.2 70.4 5.6 Ex. 5 5.1 20.1 1.2 55.7 2.6 23.3 0.9 34.9 1.1 5.2 20.4 1.4 63.1 2.4 15.3 1.0 37.8 5.9 Ex. 6 12.2 0.1 38.3 1.1 49.5 1.2 46.0 2.5 Ex. 7 0.4 0.0 72.0 0.3 26.7 0.3 62.5 3.6 Ex. 8 9.2 1.5 50.0 6.7 40.8 8.3 56.0 5.0

[0108] Wherein (for tables 1 and 2): 1) Stages of the invention. A: pheophytinisation treatment; B: treatment with zinc salt; C: treatment with a solution at pH>5; D: washes; E: packaging in brine; F: heat preservation treatment. 2) Abbreviations. FGO: fresh green olive; CSPGO: green table olive prepared in the Castelvetrano style; (i) initial; (a) stored for 6 months at 4 C.; Nd: not determined; BAS: Buffered acid solution 0.1 M Lactic acid-NaOH; AS: Unbuffered acid solution, 0.1 M HCl; BBS: Buffered base solution, 0.1 M glycine-NaOH: BS: Unbuffered base solution, 0.175 M NaOH; LAF: Lactic acid fermentation; P: Pasteurisation at 80 C. for 8 minutes; S: Sterilisation at 117 C. for 43 min. 3) The data of this example correspond to an accelerated storage test (24 h at 55 C.). 4) In this example, stage B, the treatment with zinc salt, is performed subsequent to neutralisation and at the same time as stage E, packaging in brine.

[0109] The results reveal that the conditions of storage tested may be useful for the maintenance of the desired green colour of the olives prepared Castelvetrano style, and that this improvement in colour will be intensified as the time of storage under these conditions passes. After 6 months of real storage at ambient temperature, the product displays a significant improvement in colour and may be washed, packaged and pasteurised for sale.

[0110] Phase 2. Stage D: Washes.

[0111] Immersion of the olives in tap water for 60h, with a change of water every 12 h (5 washes).

[0112] Phase 3. Stages E and F: Packaging in Brine and Heat Preservation Treatment.

[0113] Filling of 370 mL glass jars with approximately 156 g of fruits and approximately 180 mL of a buffered mix of 0.1 M lactic acid/lactate at pH 4 and containing 4% (w/v) of NaCl at a temperature of 70 C., and pasteurisation at 80 C. for 8 min.

[0114] The zinc metallochlorophyll compounds formed, responsible for the improvement in the green colour, are stable and are maintained subsequent to the heat pasteurisation treatment. In the product that had remained under treatment for 6 months, the value of the a* coordinate indicated a stabilisation of the green colour (0.27) and furthermore presented a high percentage of zinc metallochlorophyll complexes (71.63%) (FIG. 2 C.sub.2). However, the prolonged duration of the treatment and the high concentration of zinc salt caused the development of brownish patches on the product, rendering it unacceptable.

Example No. 2: Pasteurised Product Prepared in Four Phases

[0115] In this example, the pheophytinisation treatment is performed by means of a chemical process under acid conditions and is performed prior to the treatment of the vegetal products with the solution that maintains the pH of the vegetal products above 5, and to the treatment of the vegetal products with at least one divalent metal compound.

[0116] Phase 1. Stage A: Pheophytinisation Treatment with a Buffered Acid Solution:

[0117] Treatment of green table olives prepared in the castelvetrano style in a buffer solution of lactic acid/NaOH at a concentration of 0.1 M and a pH of 4, containing NaCl at 4% (w/v) and a solid:liquid ratio of 1:3 during 9 days, at an ambient temperature of 253 C.

[0118] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution.

[0119] Immersion of the fruit in a buffer mix of 0.1 M glycine/NaOH at a pH of 9.5, containing NaCl at 4% (w/v) and the food additive zinc acetate, at a concentration of 3 g/L (3000 ppm) and a solid/liquid ratio of 1:3, during 6 days, at an ambient temperature of 253 C.

[0120] Phase 3. Stage D: Washes.

[0121] Immersion of the olives in tap water for 60h, with a change of water every 12 h (5 washes).

[0122] Phase 4. Stages E and F: Packaging in Brine and Heat Preservation Treatment.

[0123] Filling of 370 mL glass jars with approximately 156 g of fruits and approximately 180 mL of a buffered mix of 0.1 M acetic acid/acetate at pH 4.3 and containing 4% (w/v) of NaCl at a temperature of 70 C., and pasteurisation at 80 C. for 8 min.

[0124] With this second example, a first optimisation of the conditions of treatment is performed. It has been revealed that the optimal pH for the formation of the metallochlorophyll complexes depends on the type of chlorophyll substrate. In the case of chlorophylls and derivatives containing Mg.sup.2+, the complexing reaction is more rapid at an acid pH, as these conditions favour the exchange of Mg.sup.2+ for 2H.sup.+ and the 2H.sup.+ for Zn.sup.2+. However, there exist bibliographic references that show that in heat-treated vegetables, wherein all the chlorophyll derivatives are of the pheophytin type (Mg.sup.2+-free), the formation of the complexes with Zn.sup.2+ is intensified at an alkaline pH. In this example, stages A and B are performed separately at different pH values, in order to reduce the time of treatment with the zinc salt. The fruit is subjected to a first acid treatment at a pH of 4 to trigger the pheophytinisation of the chlorophyll substrates (FIG. 3 C), followed by a second treatment with buffered base brine at a pH of 9.5, in the presence of 3 g/L (3000 ppm) of Zn.sup.2+ ions. After only 6 days of treatment with the zinc salt, the formation of 74.37% of zinc complexes is achieved, and a resulting stabilisation of the green colour, measured from the a* parameter, with a value of 1.53 (tables 1 and 2) The fruits are subjected to 5 washes to reduce the zinc content, and are finally packaged in acid brine and pasteurised. The complexes formed are stable to heat treatment and the green colour remains stable, but the zinc content of the product was 0.5 g/kg (503.22 ppm), 500% of the NRV.

Example No. 3: Pasteurised Product Prepared in Three Phases

[0125] In this example, the pheophytinisation treatment is performed by means of a chemical process under acid conditions and is performed prior to the treatment of the vegetal products with the solution that maintains the pH of the vegetal products above 5, and to the treatment of the vegetal products with at least one divalent metal compound Different concentrations of metal are assayed.

[0126] Phase 1. Stage A: Pheophytinisation Treatment with a Buffered Acid Solution.

[0127] Treatment of green table olives prepared in the castelvetrano style in a buffer solution of lactic/NaOH at a concentration of 0.1 M and a pH of 4, containing NaCl at 4% (w/v) and a solid/liquid ratio of 1:3 during 9 days, at an ambient temperature of 253 C.

[0128] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution.

[0129] Immersion of the fruit in a buffer mix of 0.1 M glycine/NaOH at a pH of 9.5, containing NaCl at 4% (w/v) and the food additive zinc acetate, at concentrations of 0.08 g/L; 0.1 g/L; 0.12 g/L; and 0.14 g/L (80, 100, 120, and 140 ppm) and a solid/liquid ratio of 1:1, during 48 h at ambient temperature.

[0130] Phase 3. Stages E and F: Packaging in Brine and Heat Preservation Treatment.

[0131] Filling of 370 mL glass jars with approximately 156 g of fruits and approximately 180 mL of a buffered mix of 0.1 M lactic/NaOH at pH 4.3 and containing 6% (w/v) of NaCl at a temperature of 70 C., and pasteurisation at 80 C. for 8 min.

[0132] In this third example, the quantity of zinc salt employed is reduced, which enables the elimination of the washing stage; however, a correct stabilisation of the green colour is not achieved, the values of a* remaining between 0.30 and 0.35, according to the quantity of zinc added (table 1)

Example No. 4: Sterilised Product Prepared in Two Phases

[0133] In this example, the pheophytinisation treatment is performed by means of a chemical process under acid conditions, and is carried out independently in a first phase. In a second phase, the treatment of the vegetal products with the solution that maintains the pH of the vegetal products above 5 and the treatment of the vegetal products with at least one divalent metal compound are performed simultaneously, and are thus synchronised with the heat preservation treatment.

[0134] Phase 1. Stage A: Pheophytinisation Treatment with a Buffered Acid Solution.

[0135] Treatment of green table olives prepared in the castelvetrano style in a buffer solution of lactic acid/NaOH at a concentration of 0.1 M and a pH of 4, containing NaCl at 6% (w/v) and a solid/liquid ratio of 1:3 during 9 days, at an ambient temperature of 253 C.

[0136] Phase 2. Stages B, C, E and F: Packaging in Brine at a Buffered Base pH, Addition of Zinc Salt and Heat Sterilisation Treatment.

[0137] Filling of 370 mL glass jars with approximately 156 g of fruits and approximately 180 mL of a buffered mix of 0.1 M of glycine/NaOH at pH 9.5 and containing 4% (w/v) of NaCl and the food additive zinc acetate at concentrations of 0.08 g/L; 0.1 g/L; 0.12 g/L; and 0.14 g/L (80, 100, 120, and 140 ppm) and at a solid/liquid ratio of 1:1, leaving an upper space of at least 2 mL. After 48 h of equilibrium, a technical heat sterilisation treatment is performed for at least 15 D (43 min. at 117 C.)

[0138] In this fourth example an additional optimisation is performed by combining stages B, C and E with a heat sterilisation treatment. In this way, the quantity of additive employed is reduced to 0.14 g/L (140 ppm), the washes are eliminated and the total time of preparation of the product is reduced. After the stage of treatment with acid buffer at a pH of 4 during 9 days, which causes a percentage of pheophytinisation in the chlorophyll substrates of at least 95% (FIG. 3 C), the fruits are packaged in a buffer mix at a pH of 9.5, containing different quantities of zinc, and are subjected to 15 D heat sterilisation treatment. Immediately after the heat treatment, the formation of a high percentage of zinc complexes (>43%) is achieved, as is a stabilisation of the green colour (a* between 4.28 and 5.00) (FIG. 3 D and tables 1 and 2) All the treatments achieve the desired improvement/stabilisation of the green colour and maintain a quantity of zinc in the finished product that is lower than 100% of the NRV (table 2). In the treatments with 0.08 g/L and 0.1 g/L (80 and 100 ppm) of zinc acetate, this quantity is lower than 75 ppm (75% of the NRV), the maximum quantity permitted in certain legislations (document U.S. Pat. No. 5,482,727). The product would be ready for sale in 10 days, and unlike the products of this type of preparation of heat-treated olives currently available on the market, the colour may continue to evolve favourably during the storage of the product at ambient temperature.

Example No. 5: Sterilised Product Prepared in Two Phases

[0139] In this example, the pheophytinisation treatment is performed in a first phase by means of a chemical process under acid conditions, simultaneously with the treatment of the vegetal products with at least one divalent metal compound. In a second phase, the treatment of the vegetal products with the solution that maintains the pH of the vegetal products above 5 is carried out, simultaneously with the heat preservation treatment.

[0140] Phase 1. Stages A and B: Pheophytinisation Treatment and Treatment with Zinc Salt in a Buffered Acid Solution.

[0141] Treatment of green table olives prepared in the castelvetrano style in a buffer solution of lactic acid/NaOH at a concentration of 0.1 M and a pH of 4, containing NaCl at 4% (w/v) and 0.1 g/L (100 ppm) of the food additive zinc acetate. The solid/liquid ratio is 1:1, and the treatment is 9 days at an ambient temperature of 253 C.

[0142] Phase 2. Stages C, E and F: Packaging in Brine at a Buffered Base pH and Heat Sterilisation Treatment.

[0143] Filling of 370-mL glass jars with approximately 156 g of fruits and approximately 180 mL of a buffered mix of 0.1 M of glycine/NaOH at pHs 9 and 9.5, containing 4% (w/v) of NaCl, at a solid/liquid ratio of 1:1, leaving an upper space of at least 2 mL. After 48 h of equilibrium, a technical heat sterilisation treatment is performed for at least 15 D (43 min. at 117 C.).

[0144] In this fifth example an additional optimisation is performed by combining stages A and B (treatment in buffered acid solution and treatment with zinc salt). In this way an even further reduction in the quantity of zinc added to the product is achieved, reaching <40 ppm (table 2), forming a lower quantity of metallochlorophyll complexes than that of the previous example (between 15 and 23%), but sufficient to stabilise the green colour, with an a* value of between 2.54 and 3.26. In this case, due to adding the zinc at the acid treatment stage, the degree of pheophytinisation of the chlorophyll pigments was lower, maintaining subsequent to the heat treatment 20% of the native complexes with magnesium.

Example No. 6: Sterilised Product Prepared in Three Phases

[0145] In this example, the pheophytinisation treatment is performed in a first phase by means of a chemical process under acid conditions, and in a second phase the treatment of the vegetal products with at least one divalent metal compound is performed simultaneously with the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5.

[0146] Raw Material:

[0147] A 5-kg batch of olives of the cacerea variety was subjected to a treatment with a solution of NaOH at 1.7% (w/v) containing 3% (w/v) of NaCl. The fruit/liquid ratio was 4:3 and the duration of the treatment was 6.5 hours. Subsequently, they were washed in water for 4 hours at the same fruit/liquid proportion.

[0148] Phase 1. Stage A: Pheophytinisation Treatment by a Chemical Process Under Acid Conditions.

[0149] Treatment of the olives with a 0.1 M solution of HCl and 8% NaCl (w/v) at a fruit/liquid ratio of 4:3 during 4 days.

[0150] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution:

[0151] Treatment of the olives with a buffered solution of glycine-NaOH 0.1 M at a pH of 9.5, containing 0.2 g/L (200 ppm) of Zn (II) and a fruit/liquid ratio of 4:3 during 48 hours.

[0152] Phase 3. Stages E and F: Packaging in Brine and Heat Sterilisation Treatment.

[0153] Filling of 370-mL glass jars with approximately 200 g of fruits and approximately 150 mL of NaCl brine at 4% (w/v) at a solid/liquid ratio of 4:3, leaving an upper space of at least 2 mL, and technical heat sterilisation treatment for at least 15D (43 min. at 117 C.).

[0154] In this example stage A is optimised, replacing the buffered 0.1 M solution of lactic acid-NaOH at a pH of 4, employed in the previous examples, by an unbuffered 0.1 M acid solution of hydrochloric acid (pH=1.8). By subjecting the fruits to a much more intense acid treatment, the duration of this first stage is reduced from the 9 days required in the examples above to 4 days, and furthermore, the quantity of liquid necessary for the optimal performance of this stage is also reduced. On conclusion of these 4 days, the a* coordinate was established at 3.630.35 and the percentage of pheophytinisation reached 100% of the chlorophyll fraction of the fruit.

[0155] After the phase of adding the zinc salt at a base pH, once the olives were packaged, they displayed a significant improvement in their green colour after the heat treatment, materialised in a variation of the a* coordinate, which stood at 4.230.33, and a 50% formation of zinc metallochlorophyll complexes (Tables 1 and 2).

Example No. 7: Sterilised Product Prepared in Three Phases

[0156] In this example, the pheophytinisation treatment is performed in a first phase by means of a chemical process under acid conditions, and in a second phase the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5 is performed, and in a third phase the treatment of the vegetal products with at least one divalent metal compound is performed.

[0157] Raw Material:

[0158] A 5-kg batch of olives of the cacerefia variety was subjected to a treatment with a solution of NaOH at 1.7% (w/v) containing 3% (w/v) of NaCl. The fruit/liquid ratio was 4:3 and the duration of the treatment was 6.5 hours. Subsequently, they were washed in water for 4 hours at the same fruit/liquid proportion.

[0159] Phase 1. Stage A: Pheophytinisation Treatment by a Chemical Process Under Unbuffered Acid Conditions.

[0160] Treatment of the olives with a 0.1 M solution of HCl and 8% NaCl (w/v) at a fruit/liquid ratio of 4:3 during 4 days.

[0161] Phase 2. Stage C: Treatment in an Unbuffered Base Solution to Maintain the pH >5:

[0162] Treatment of the olives with a 0.175 M solution of NaOH during 24 h to reach a pH value >5.

[0163] Phase 3. Stages B, E and F: Treatment with Zinc Salt, Packaging in Brine and Heat Sterilisation Treatment.

[0164] Filling of 370-mL glass jars with approximately 200 g of fruits and approximately 150 mL of NaCl brine at 4% (w/v), containing 0.1 g/L (100 ppm) of Zn (II) at a fruit/liquid ratio of 4:3 during 24h, leaving an upper space of at least 2 mL, and technical heat sterilisation treatment for at least 15D (43 min. at 117 C.).

[0165] In this example, stage A is performed as in the previous case, with an unbuffered acid solution, and stage C is optimised, replacing the buffered 0.1 M glycine-NaOH solution employed in the previous examples by an unbuffered base solution of 0.175 M of sodium hydroxide (pH=13). By subjecting the fruits to a much more intense base treatment, the duration of this stage is reduced to 24h.

[0166] On conclusion of the 4 days of pheophytinisation (stage A), the a* coordinate stood at 4.280.22 and the percentage of chlorophyll derivatives with 2H.sup.+ reached 100% of the chlorophyll fraction of the fruit.

[0167] After the neutralisation phase with unbuffered base solution, the fruits are packaged in brine containing the zinc salt and are subjected to heat treatment. After the heat treatment, the fruits presented a significant improvement in their green colour, the a* coordinate reaching a value of 4.470.55 and a formation of zinc metallochlorophyll complexes of 26.70.3% (Tables 1 and 2). By including the zinc in the packaging brine, the quantity of salt employed is reduced by half.

Example No. 8: Sterilised Product Prepared in Three Phases

[0168] In this example, the pheophytinisation treatment is performed in a first phase by means of a biotechnological fermentation process, and in a second phase the treatment of the vegetal products with at least one divalent metal compound is performed simultaneously with the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5.

[0169] Raw Material:

[0170] A 5-kg batch of olives of the hojiblanca variety was subjected to treatment with a solution of NaOH at 1.7% (w/v) containing 3% (w/v) of NaCl. The fruit/liquid ratio was 4:3 and the duration of the treatment was 6.5 hours. Subsequently, they were washed in water for 4 hours at the same fruit/liquid proportion.

[0171] Phase 1. Stage A: Pheophytinisation Treatment by a Biotechnological Fermentation Process:

[0172] Treatment of the raw material by means of a natural lactic-acid fermentation, performed in NaCl brine at an equilibrium concentration of 7%, during a period of 3 months, at a solid/liquid ratio of 4:3.

[0173] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution:

[0174] Treatment of the olives with a 0.1 M buffered solution of glycine-NaOH at a pH of 9.5, containing 0.2 g/L (200 ppm) of Zn (II) at a fruit/liquid ratio of 4:3 during 48 hours.

[0175] Phase 3. Stages E and F: packaging in brine and heat sterilisation treatment.

[0176] Filling of 370-mL glass jars with approximately 200 g of fruits and approximately 150 mL of NaCl brine at 4% (w/v) at a solid/liquid ratio of 4:3, leaving an upper space of at least 2 mL, and technical heat sterilisation treatment for at least 15D (43 min. at 117 C.).

[0177] The purpose of this example is to test the possibility of performing Stage A by means of a lactic-acid fermentation which lowers the pH to below 4, due to the generation of lactic acid caused by the fermentation of the sugars present in the olives.

[0178] This variant is of great interest for companies of the table olive sector, as the preparation of olives in the Spanish or Sevillian style by means of lactic-acid fermentation and their subsequent packaging in acid brine is one of the most widespread practices in the sector, which enables the availability of this type of product almost all the year round. By means of this biotechnological process, olives of a yellowish colour are obtained, with an a* coordinate of 2.430.05 and a percentage of pheophytinisation that reached 100% of the chlorophyll fraction. This result proves the efficacy of the lactic-acid fermentation process in pheophytinising the chlorophyll initially present in the olives. This may also be applicable to any type of green vegetable or fruit preserved by means of acid fermentation.

[0179] In this example, applied to olives, subsequent to the phase of adding zinc salt at a base pH, once the product was packaged it presented a significant improvement in the green colour after the heat treatment, materialised in a variation in the a* coordinate, which stood at 3.960.11, and a formation of zinc metallochlorophyll complexes of 41% (Tables 1 and 2).

Examples 9 (A and B) and 10 (A and B)

[0180] In these examples, the pheophytinisation treatment is performed in a first phase by means of heating, and in a second phase the treatment of the vegetal products with at least one divalent metal compound is performed simultaneously with the treatment of the vegetal products with the solution that maintains the pH of the vegetal products at a value above 5.

[0181] Raw Material.

[0182] The invention is applied to the preparation of a typical green vegetable (green bean). In these examples, the embodiment of the pheophytinisation treatment (stage A) is a heat treatment, performed with two variants: A) physical treatment of boiling in water, and B) physicochemical treatment of boiling in water acidified with 0.125% of citric acid.

[0183] The fresh green beans were cut into pieces of about 3 cm and were washed in tap water. Next, approximately 400 g of the vegetal material was boiled in a basin containing 1.6 L of the boiling liquid, at a temperature of 95-97 C. during 20 min.

Examples Nos. 9A and 9B: Pasteurised Product Prepared by Double Boiling in Three Phases

[0184] In these examples, after the pheophytinisation stage, the product (200 g) was subjected to an additional boiling in a 0.1 M buffer mix of glycine/NaOH at a pH of 8, containing Zn (II) at a concentration of 0.2 g/L (200 ppm) and at a product/liquid ratio of 1:4, during 45 min. at 95-97 C. Finally, the product was packaged in a liquid consisting of acid brine at a pH of <4.6, and the heat pasteurisation treatment was performed.

[0185] Phase 1. Stage A: Pheophytinisation Treatment by a Physical Heating Process:

[0186] Blanching in water at 95-97 C. with green beans, cut into pieces and washed, at a solid/liquid ratio of 1:4 for 20 min.

[0187] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution.

[0188] Immersion of the fruits in a 0.1 M buffer mix of glycine/NaOH at a pH of 8, containing zinc acetate at a concentration of 0.2 g/L (200 ppm) and at a solid/liquid ratio of 1:4, for 45 minutes at 95-97 C.

[0189] Phase 3. Stages E and F: Packaging in Brine and Heat Preservation Treatment.

[0190] Filling of 370-mL glass jars with approximately 200 g of vegetal matter and approximately 150 mL of NaCl brine at 3% (w/v), containing 0.6% of lactic acid at a temperature of 70 C., followed by a heat pasteurisation treatment at 90 C. for 15 min.

[0191] The entire performance of the process yields a correct stabilisation of the green colour, both in the product boiled in water (a*=6.760.503) and that boiled in acidified water (a*5.850.11), reaching a percentage of Zn.sup.2+ metallochlorophyll complexes of 25.85 and 28.42% respectively (tables 3 and 4 and FIG. 4).

[0192] Conversely, the product prepared in the traditional way, without the addition of zinc salt, by boiling in water, packaging in acidified brine and subsequent pasteurisation, presented a significant loss of green colour (a*=1.41) due to the replacement of Mg.sup.2+ by 2H in the entirety of the chlorophyll pigments (tables 3 and 4 and FIG. 4B).

[0193] These examples illustrate how the process of the present invention provides significant improvements with regard to other prior processes, as the complexing reaction of the pigments with the divalent metal being more efficient, an ideal fruit or vegetable product with a medium-low chorophyllic derivative content may be obtained, employing a much lower quantity of zinc than that employed in other processes. For example, in document U.S. Pat. No. 6,004,601A, a blanching solution with at least 500 ppm of zinc is used, with a vegetable:blanching solution ratio of 1:12; that is, 6000 mg of zinc for each kg of vegetables, while in the examples described herein 800 mg are used for each kg of vegetables (buffered base solution with 200 ppm in a vegetable:brine solution ratio of 1:4).

[0194] Neither is a combined addition of copper salts necessary, as indicated in document U.S. Pat. No. 5,114,725 A. Thus, the green colour of the vegetal product is stabilised prior to the heat preservation treatment, enabling its packaging under acid conditions. To ensure the long-term safety of the product, a heat pasteurisation treatment is therefore sufficient, this being less aggressive than the required sterilisation applied in other patented processes (4473591; U.S. Pat. No. 5,114,725 A; 5482727 and U.S. Pat. No. 6,004,601A), reducing to the maximum the issues concerning texture and cooked taste. The product obtained in these preferred embodiments contains 15310% and 14410% of the NRV per 100 g of product.

Examples Nos. 10A and 10B: Pasteurised Product Prepared in Three Phases

[0195] In this example, after the pheophytinisation stage, the product (200 g) was treated with a 0.1 M buffer mix of glycine/NaOH at a pH of 8, containing 0.2 g/L (200 ppm) of Zn (II) but reducing the solid:liquid ratio to 4:3 and maintaining the product at a controlled temperature of 60 C. for 5 days. Finally, the original brine was replaced by an acid brine at a pH of <4.6, and the heat pasteurisation treatment was performed.

[0196] Phase 1. Stage A: Pheophytinisation Treatment by a Physical Heating Process:

[0197] Blanching treatment of cut, washed green beans in water at 95-97 C., at a solid/liquid ratio of 1:4 during 20 min.

[0198] Phase 2. Stages B and C: Treatment with Zinc Salt in a Buffered Base Solution.

[0199] Immersion of the vegetal matter in a 0.1 M buffer mix of glycine/NaOH at a pH of 8, containing zinc acetate at a concentration of 0.2 g/L (200 ppm) and at a solid/liquid ratio of 4:3, for 5 days at a controlled temperature of 601 C.

[0200] Phase 3. Stages E and F: Packaging in Brine and Heat Preservation Treatment.

[0201] Filling of 370-mL glass jars with approximately 190 g of vegetal matter and approximately 130 mL of a NaCl brine at 3%, containing 0.6% (w/v) of lactic acid at a temperature of 70 C., and pasteurisation at 90 C. for 15 min.

[0202] With this process, subsequent to Phase 1, a percentage of pheophytinisation of the chlorophyll fraction of the vegetal matter reaching 82.86% is achieved in the case of boiling in water, and 93.57% in the case of boiling in acidified water. The entire performance of the process yields a correct stabilisation of the green colour (tables 3 and 4 and FIG. 4A), both in the product boiled in water (a*=5.810.23) and that boiled in acidified water (a*-5.460.41), reaching a percentage of Zn.sup.2+ metallochlorophyll complexes of 33.03 and 32.35% respectively. However, the quantity of zinc incorporated differentiated the two embodiments. When the prior pheophytinisation stage is performed in water (example 10A), the zinc content (63.133.61 ppm) was lower than that obtained when the pheophytinisation is performed in acidified water (86.452.62 ppm) (example 10B). In any case, in both embodiments a product is obtained with ideal organoleptic characteristics with no need to exceed 100% of the NRV per 100 g of product. By reducing the temperature at which the treatment with zinc salt is performed, likewise the solid:liquid ratio, one achieves, in addition to the advantages mentioned in the above examples (9A and 9B), a considerable reduction in the quantity of zinc employed, to 150 mg per kg of product (a solution of 200 ppm of zinc at a vegetable:brine ratio of 4:3) and also in the quantity of mineral that is incorporated into the product.

TABLE-US-00004 TABLE 3 Chromatic coordinate a* in green beans processed according to different examples of the invention. Sample Stages of the invention.sup.1) a* FGB.sup.2) 10.51 0.36 A pH of the vegetable BOIL initial final B C D E F BGBC A 5.8 5.8 3.03 0.16 B 5.8 4.5 2.19 0.18 BPGBC A 5.8 5.8 P 1.41 0.17 B 5.8 4.5 P 1.59 0.42 Ex. 9A A 5.8 5.8 BBS pH 8 + 200 ppm of No P Ex. 9B B 5.8 4.5 Zn.sup.2+ at 95-97 C. during 45 No P 5.85 0.11 min. (1:4) Ex. 10A A 5.8 5.8 BBS pH 8 + 200 ppm of No P 5.81 0.81 Ex. 10B B 5.8 4.5 Zn.sup.2+ during 5 days at No P 5.46 0.80 60 C. (4:3)

TABLE-US-00005 TABLE 4 Percentage of chlorophyll pigments with Mg, with 2H and with Zn, and zinc content, in green beans processed in accordance with different examples of the invention, as described in table 3. Chlorophyll pigment (%) Zinc content Sample with Mg with 2H.sup.+ with Zn.sup.2+ (ppm) FGB.sup.2) 98.23 3.31 1.77 0.88 Nd BGBC 17.1 1.6 82.96 9.4 0 Nd 6.4 1.2 93.67 4.4 0 BPGBC 0 100.0 0.0 0 2.8 0.1 0 100.0 0.0 0 Ex. 9A 0 74.25 7.2 25.95 2.9 152.8 10.3 Ex. 9B 0 71.6 8.6 28.4 3.7 144.2 10.0 Ex. 10A 3.29 0.9 63.8 6.6 33.0 6.8 63.1 3.6 Ex. 10B 2.4 0.5 65.2 4.2 32.3 3.6 86.55 2.6

[0203] Wherein (for tables 3 and 4): 1) Stages of the invention. A: pheophytinisation treatment; B: treatment with zinc salt; C: treatment with a solution at pH >5; D: washes; E: packaging in brine; F: heat preservation treatment; 2) Abbreviations. FGB: fresh green bean; BGBC: boiled green bean control; BPGBC: boiled and pasteurised green bean control; BOIL: Boiling during 20 min. at 95-97 C. at a solid:liquid proportion (1:4); A: in water at a pH of 7.6; B: in water+0.125% citric acid (pH 2.77); BBS: 0.1 M glycine-NaOH buffered base solution; P: 15-minute pasteurisation at 90 C. in NaCl brine at 3% with 0.6% lactic acid; Nd: Not determined.