METHODOLOGY FOR PREPARING ETHANOL-REDUCED FERMENTED BEVERAGES

Abstract

The present invention is directed to a generic methodology for preparing wines and other beverages having reduced ethanol content, where said wines or beverages may be sweet, dry or demi-sec beverages. The methodology comprises different fermentation stages, wherein wine yeasts Pichia anomala y Saccharomyces sp. are used. The present invention teaches a methodology, in which yeast groups are used, and said groups are capable of generating several yields of ethanol production by controlling critical variables in the production of an organoleptically acceptable wine through a minor intervention in the aromatic compounds and the final product, resulting in a wine of similar features to those ones available in the market, which has the antioxidant properties and the quality of traditional wines, with lower alcoholic content.

Claims

1. A method for preparing alcohol-reduced alcoholic beverages, CHARACTERIZED in that: a) the must is inoculated with non-Saccharomyces yeasts; b) a first oxidative stage of biomass growth is carried out; c) the yeast strain of stage (b) is removed, and d) a second fermentative stage is carried out by inoculating with Saccharomyces yeasts.

2. A method according to claim 1, CHARACTERIZED in that the concentration of non-Saccharomyces yeast inoculum ranges from 0.1 g/L to 0.4 g/L.3.

3. A method according to claim 2, CHARACTERIZED in that the inoculum must be previously activated with an alginic solution.

4. A method according to claim 1, CHARACTERIZED in that the stage described in (b) corresponds to a culture with micro-oxygenation.

5. A method according to claim 4, CHARACTERIZED in that in the micro-oxygenation described in (b) the dissolved oxygen remains throughout the process at a concentration of about 0.1 to 1 vvm.

6. A method according to claim 1, CHARACTERIZED in that the stage described in (b) uses a yeast strain, in which glycolytic metabolism generates a reduced production of alcohol.

7. A method according to claim 6, CHARACTERIZED in that the stage described in (b) corresponds to a fermentation of a P. anomala strain.

8. A method according to claim 1, CHARACTERIZED in that the stage described in (b) is carried out at a temperature of from 12 C. to 19 C.

9. A method according to claim 1, CHARACTERIZED in that the removal of the yeast in stage (c) is carried out by decantation.

10. A method according to claim 1, CHARACTERIZED in that in the stage described in (d) the concentration of Saccharomyces yeast inoculum ranges from 0.1 g/L to 0.4 g/L.

11. A method according to claim 10, CHARACTERIZED in that the stage described in (d) corresponds to an anaerobic culture.

12. A method according to claim 11, CHARACTERIZED in that the culture must be kept below 4 mg/L of dissolved oxygen.

13. A method according to claim 10, CHARACTERIZED in that the stage described in (d) corresponds to a fermentation of a Saccharomyces sp. strain.

14. A method according to claim 10, CHARACTERIZED in that the stage described in (d) is carried out at a temperature of from 10 C. to 17 C.

15. A method according to claim 1, CHARACTERIZED in that, optionally, if the must contains grape pomace a devatting and pressing stage is carried out in order to remove grape skins.

16. A method according to claim 15, CHARACTERIZED in that the devatting and pressing stage is carried out by a pressing machine through mechanical action.

17. A method according to claim 1, CHARACTERIZED in that the resulting product is micro-filtered to remove all microorganisms contained in the ferment.

18. A method for preparing alcohol-reduced alcoholic beverages, CHARACTERIZED in that it is carried out in two differential stages using a group of yeasts: in a first oxidative stage non-Saccharomyces yeast is used, whereas the subsequent second fermentative state uses Saccharomyces yeast.

19. A method according to claim 18, CHARACTERIZED in that a group of yeasts is used, which is capable of generating different yields of ethanol production and providing distinct organoleptic features.

20. A method for preparing ethanol-reduced wine, CHARACTERIZED in that it comprises the stages of: a) the must is inoculated with non-Saccharomyces yeasts; b) a first oxidative stage of biomass growth is carried out; c) the yeast strain of step (b) is removed, and d) a second fermentative stage is carried out by inoculating with Saccharomyces yeasts.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0012] FIG. 1 is a graphical demonstration of the kinetics of fermentation obtained from must of Muscat of Alexandria grapes. (.circle-solid.), consumption of glucose. (.square-solid.), increase of biomass in the inside of the reactor.

[0013] FIG. 2 represents a comparison of the alcohol content (in % v/v of ethanol) obtained at the end of the process for three different fermentations. The negative control corresponds to most from Alexandria muscatel grape with constant aeration. The positive control corresponds to Moscatel grape without aeration. The test corresponds to a fermentation carried out by the methodology described herein starting from the same must used in the above-described processes.

[0014] FIG. 3 shows the kinetics of fermentation by using concentrated red grape must. (.square-solid.), reducing sugars. (.box-tangle-solidup.), cellular biomass. (), pH throughout the process. () concentration of ethanol comprised in the ferment.

[0015] FIG. 4 represents a comparison of the alcohol content (in % v/v of ethanol) obtained at the end of the process for three different fermentations. The negative control corresponds to concentrated grape most with constant aeration. The positive control corresponds to concentrated grape must without aeration. The test corresponds to a fermentation carried out by the methodology described herein starting from the same must used in the above-described processes.

SUMMARY OF THE INVENTION

[0016] The present invention represents a generic methodology for preparing wines and other beverages having reduced ethanol content, where said wines or beverages may be sweet, dry or demi-sec beverages. The methodology comprises different fermentation stages, wherein wine yeasts Pichia anomala y Saccharomyces sp. are used.

[0017] The present invention teaches a methodology, in which yeast groups are used, and said groups are capable of generating several yields of ethanol production by controlling critical variables in the production of an organoleptically acceptable wine through a minor intervention in the aromatic compounds and the final product, resulting in a wine of similar features to those ones available in the market, which has the antioxidant properties and the quality of traditional wines, with lower alcoholic content.

DETAILED DESCRIPTION OF THE INVENTION

[0018] As it is known, according to the above-indicated background, one of the main problems the wine industry is currently facing is the change of preferences of consumers, which increasingly prioritize the intake of beverages with low or no alcohol content.

[0019] Considering the importance that the health benefits must be strictly linked to the satisfaction of the tasting, the present invention is worded, which considers both key factors for success in product sales. This innovation is based on the implementation of a fermentation carried out in two differential stages. The first stage consists on a micro-oxygenation process, which promotes the growth of P. anomala biomass, metabolizing the glucose by oxidative routes having a minimum production of alcohol. In the second stage of the fermentation a replacement of the yeast strain is made by removing the Pichia ferment and inoculating with Saccharomyces sp., micro-organism that provides the characteristic finish to the wine. As previously mentioned, non-Saccharomyces yeasts secrete a higher concentration of enzymes to the environment that improve the organoleptic features of fermented beverages, so during the development of the present invention a non-Saccharomyces species was used as micro-organism responsible for the primary stage of this methodology. Thus, the methodology suggested herein uses Pichia anomala, which is a micro-organism having a behavior strongly influenced by oxygen limitation, and not by the concentration of glucose present in the medium for ethanol production, strongly decreasing the expression of the alcohol dehydrogenase enzyme (EC. 1.1.1.1) under aerobic conditions.

[0020] However, despite that P. anomala has been used for vinification processes with good results, these have been mostly red wines that lack the characteristic wine finish in the light of oenologists' opinion.

[0021] As this is a methodology applicable for all types of wines, including white, ros and red wines, it is of great importance to use in the manufacture process yeast appropriate to this goal. For this reason, in order to implement the final stage of fermentation, a strain of Saccharomyces sp. has been chosen as the most suitable for this purpose, so that in the final stage of the methodology a time of fermentation with Saccharomyces sp. is involved, microorganism capable of producing intense floral notes that increase wine aromatic complexity.

[0022] Advantages

[0023] Unlike existing processes, the present invention provides a fermented beverage that does not require dealcoholization, which allows obtaining a beverage low in alcohol at lower cost, maintaining its organoleptic properties, without reducing the quality thereof.

[0024] Mechanism of Action

[0025] The present invention comprises differential stages of fermentation in order to be capable of handling the metabolism of the involved micro-organisms by controlling the external variables.

[0026] Glucose can be metabolized in yeasts by two different routes: oxidative route or fermentative one. The objective of the methodology of the present invention is to promote the oxidative respiration route, thus promoting the metabolism, which leads to the biomass generation, an increase in cell growth with minimum ethanol production and the generation of other compounds of wine interest. To carry out the above-mentioned process, the application of oxygen in stage I of fermentation is required; thus, Pichia anomala, which is a negative Crabtree yeast cultured in aerobic conditions, metabolizes glucose preferably through pyruvate dehydrogenase to acetyl-CoA. Subsequently, this molecule enters the Krebs cycle to its complete oxidation and the consequent generation of energy required for the processes that lead to its duplication (Van Dijken et al., 1993; Gancedo & Serrano 1989). This is due to the fact that under these conditions this molecule shows minimum levels of transcription of the enzyme pyruvate decarboxylase (EC. 4.1.1.1), so the metabolic pathway leading to the formation of ethanol from acetaldehyde is limited (Postma et al., 1989).

[0027] Another important feature that influences on the selection of this strain for the aerobic fermentation is that under these growth conditions P. anomala generates a high yield of biomass and, furthermore, it is able to generate other important compounds for the organoleptic properties of the wine, such as glycerol and acetate, with a marginal synthesis of ethanol.

[0028] One of the last stages of the methodology for the preparation of reduced wine into ethanol consists in an anaerobic fermentation carried out by Saccharomyces sp. yeast. This stage is of great enological importance, since this micro-organism provides high concentrations of glycerol, without increasing the acetic acid, and an increase in the production of certain secondary aromas, thus improving the body and flavor of the wine.

[0029] Methodology

[0030] 1. Must Processing

[0031] After obtaining the must by stemming and crushing the fruiteither if it corresponds to grape juice to produce white, ros or red wine, this shall be stored in a container, for example a metal container, stainless steel, plastic or wood at a temperature between 5 C. to 4 C. until the use thereof.

[0032] If the must is not under aseptic conditions, the necessary treatment should be executed in order to decrease the load of native yeasts that could be comprised in suspension by chemical processes, such as addition of antifungal and antibacterial agents or by physical processes such as microfiltration, centrifugation or decantation.

[0033] 2. Activation of the Pichia anomala Strain

[0034] In case Pichia anomala comes directly from a culture suitable for its growth as liquid or solid YM medium (Yeast extract-Malt extract Medium), YPD (Yeast Extract Peptone Dextrose Medium) or another medium for yeasts supplemented with glycerol 1-10%, it must be collected by any method of decantation, for example, centrifugation, re-suspended and washed with sterile distilled water as many times as necessary. The pellet obtained from the last wash must be moisturized gently in a solution of sodium alginate from 3 mM to 7 mM, at a range of 20-30 C. and pH 4-7. Then it must stand for about 10 to 25 minutes until the use thereof.

[0035] 3. FermentationStage I

[0036] This first stage consists on aerobic fermentation. Therefore, an aeration system is mounted, which consists of an external air supply and a diffuser. During the entire process the dissolved oxygen must remain to a concentration of between 0.1-1 vvm. To do this, the flow of air intake to the fermentation vessel must be regulated as the culture becomes denser.

[0037] The must shall be inoculated with Pichia anomala. The yeast concentration in the must shall be greater than 0.1 g/l and less than 0.4 g/L, preferably 0.25 grams of dry yeast per liter of water. Gently add the required volume in the must, trying to homogenize well through some mechanical method. Fermentation shall be carried out throughout the process at a temperature ranging from 12 C. to 19 C. The concentration of sugar in the must shall be recorded periodically (recommended between 6, 16 or 24 hours) by physical methods such as refractometry or by chemical and spectrophotometric methods such as DNS (method of 3.5 dinitrosalicylic acid). Aeration must be stopped when the yeast achieves between 25-40 g/l of residual sugar, preferably 30 g/L.

[0038] 4. Activation of Saccharomyces sp. Strain

[0039] In case Saccharomyces sp. comes directly from a culture suitable for its growth as liquid or solid YM medium, YPD or another medium for yeasts culture, it must be collected by any method of decantation such as centrifugation, re-suspended and washed with a sterile solutes-free solution as many times as necessary. The pellet obtained from the last wash must be moisturized gently in sterile, demineralized and distiller water, at a temperature ranging from 30 C. to 40 C., and then it stands for about 10 to 20 minutes until the use thereof.

[0040] 5. FermentationStage II

[0041] The must shall stand long enough to decant the microorganisms contained therein and the period of time recommended ranges about 18 to 24 hours. Alternatively, an agent accelerating the decanting process may be added, such as bentonite according to the proportions indicated by the manufacturer. The precipitate formed shall be removed by suction, filtration or any physical method appropriate to eliminate the existing micro-organisms (P. anomala) and residues originated by the must. In case said processes are not enough microfiltration should be carried out. As soon as it is finished, the aeration is stopped and it is inoculated with Saccharomyces sp. The yeast concentration in the must shall be greater than 0.2 g/l and less than 0.7 g/L, preferably 0.25 grams of dry yeast per liter of water. Gently add the required volume in the must, trying to homogenize well through some mechanical method.

[0042] 6. Devatting and pressing

[0043] In the case of wine, in which fermentation is carried out in the presence of grape pomace (mainly in varieties of ros and red wines) the stage of devatting is required, wherein through treatment or mechanical operations (the use of press machine is recommended to decrease the presence of exogenous micro-organisms) grape pomace is removed from the deposits of the useful and fermented liquid.

[0044] 7. Decanting

[0045] The wine should be micro-filtered to remove all microorganisms contained in the ferment. The use of membrane filters, where the executor must choose the most suitable one according to their conditions and volumes of product, is recommended.

USE EXAMPLES

Example 1

[0046] The must elaborated from Muscat of Alexandria grapes by stemming and subsequent crushing of the grapes is deposited in a fermentation vessel made of stainless steel, which was previously sterilized by moist heat.

[0047] Depending on the concentration of yeast intended to be obtained, hours before inoculation with Pichia anomala it is necessary to start a culture thereof in liquid medium YM (3 g/L of yeast extract, 3 g/L of malt extract, soy, 5 g/L of soy peptone, 10 g/L of glucose) for the production of biomass. Just before the use thereof, the culture must be collected by centrifugation at 5,000 RPM, re-suspended in sterile and distilled water, and washed three times. Subsequently it is gently moisturized with an alginic solution 4.5 mM, since as it is a liquid culture, a proper activation is not required, but the incubation in the presence of alginate. It stands for 20 minutes at 28 C.

[0048] The first stage of fermentation consists on aeration of the medium, which increases throughout the process to maintain a constant dissolved-oxygen concentration at 10 mg/L. At the beginning, and after 72 hours the fermentation begins, the process must be controlled every 10 hours in order to quantify the concentration of consumed sugar and the generated biomass (FIG. 1). Aeration is stopped when the yeast achieves 45 g/l of residual sugar.

[0049] Once the peak of sugars is reached, aeration is stopped, and the ferment decants for 20 hours. In the meantime, a Saccharomyces sp. strain is activated as well as P. anomala, but at a temperature of 38 C. As soon as the above-specified time passes, it is necessary to remove the muddy bottom of the bottom of the fermentation vessel by opening the bottom valve thereof. It is inoculated with Saccharomyces and the process is completed in additional 50 hours under an anaerobic environment.

[0050] Since the fermentation is carried out without the presence of grape pomace, the devatting consists on a centrifugation at 5,000 RPM, during 12 minutes, and then it is micro-filtered using 0.22 m filters.

[0051] The concentration of ethanol produced at the end of the fermentation was considerably lower compared to the positive control, achieving a decrease of 53% (FIG. 2).

Example 2

[0052] The fermentation was carried out from red-grapes concentrated must. Pichia anomala was grown during 96 hours in a YM-glycerol medium (3 g/L of yeast extract, 3 g/L of malt extract, 5 g/L of soy peptone, 10 g/L of glucose, 5% of glycerol) for the production of biomass. Just before the use thereof, the culture must be collected by centrifugation at 5,000 RPM, re-suspended in sterile and distilled water, and washed three times. Subsequently, it is gently moisturized with an alginate solution 4.5 mM. It stands for 20 minutes at 28 C.

[0053] The first stage of fermentation consists on aeration of the medium, which increases throughout the process to maintain a constant dissolved-oxygen concentration at 10 mg/L. At the beginning, and after 72 hours the fermentation begins, the process must be controlled every 10 hours in order to quantify the concentration of consumed sugar and the generated biomass (FIG. 3). Aeration is stopped when the yeast achieves 32 g/l of residual sugar.

[0054] Once the peak of sugars is reached, aeration is stopped, and the ferment decants for 20 hours. In the meantime, a Saccharomyces sp. strain is activated as well as P. anomala, but at a temperature of 38 C. supplemented with 1% of glycerol. As soon as the above-specified time passes, it is necessary to remove the muddy bottom of the bottom of the fermentation vessel by opening the bottom valve thereof. It is inoculated with Saccharomyces and the process is completed in additional 50 hours under an anaerobic environment.

[0055] The devatting consists on a centrifugation at 5,000 RPM, during 12 minutes, and then it is micro-filtered using 0.22 m filters.

[0056] As in Example 1, the concentration of ethanol produced at the end of the fermentation was considerably lower compared to the positive control, which in this case achieved a decrease of 40% (FIG. 4).