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Article

Difficulties Associated with Small-Scale Production of Carbonic Maceration Wines

by
Pilar Santamaría
,
Lucía González-Arenzana
,
Rocío Escribano-Viana
,
Patrocinio Garijo
,
Rosa López
,
Susana Sanz
and
Ana Rosa Gutiérrez
*
ICVV, Instituto de Ciencias de la Vid y el Vino (Universidad de La Rioja, Gobierno de La Rioja, CSIC), Finca La Grajera, Ctra. LO-20-Salida 13, 26071 Logroño, Spain
*
Author to whom correspondence should be addressed.
Fermentation 2022, 8(1), 27; https://doi.org/10.3390/fermentation8010027
Submission received: 14 December 2021 / Revised: 4 January 2022 / Accepted: 5 January 2022 / Published: 10 January 2022
(This article belongs to the Section Fermentation for Food and Beverages)

Abstract

:
The aim of the work was to study the vinification by carbonic maceration carried out in small volume tanks, because the use of these deposits is necessary in scientific studies where repetitions are mandatory. For this, vinifications were carried out in 300-kg tanks with grapes of the Tempranillo variety. We studied the development of the alcoholic and malolactic fermentations and the microorganisms responsible for them. The results showed an alteration of the wines as a result of the low levels of yeast and the huge bacteria population. This was probably due to the difficulty in maintaining the necessary temperature and anaerobic conditions in the small tanks employed.

1. Introduction

Vinification by carbonic maceration (CM) involves the process whereby the whole grapes are subjected to anaerobic conditions [1]. When the grapes are placed in a carbon dioxide (CO2)-enriched medium, they immediately change from a respiratory metabolism to an anaerobic fermentative metabolism called intracellular fermentation (IF). For this reason, in CM the intact grape clusters, without destemming or crushing, are placed into tanks and kept under a CO2 atmosphere. Some grapes located in the lower zone of the tank are crushed by the weight and pressure produced by the ones above and release must to the bottom of the tank. This released must is fermented by yeasts. Under anaerobic conditions, the IF is carried out by grape enzymes inside the whole berries, triggering the production of alcohol, the degradation of malic acid, pectolytic, and proteolytic phenomena, the formation of volatile compounds, and the diffusion of phenolic compounds from the skin to the pulp [2]. As a result of these processes, the whole grapes, at a certain moment, split open and release their juice into the tank, increasing the liquid phase, which continues to fermenting due to the yeasts. Therefore, the IF of the grapes and the alcoholic fermentation (AF) of the must by yeasts occur simultaneously in the tank. After this first phase, drawing off is done by racking a free-run, partly fermented wine, and the grapes that remain whole are pressed to release a higher-density press-wine. Then, a second phase begins when both wines—mixed or separate—complete their AF by the presence of yeast and the malolactic fermentation (MLF) by lactic acid bacteria (LAB).
CM winemaking is typically used in different European regions such as Beaujolais in France, Vino novello in Italy, and Cosechero wine in La Rioja, Spain. Although CM wines are recognized as high quality young wines, recent works that describe their physicochemical and microbiological characteristics are scarce and contradictory. The contradictory results could be due to a wide range of causes such as the grape variety, the grape ripeness level, the vintage, or the winemaking conditions [3,4,5]. Therefore, it is paradoxical that being a traditional processing system and widely used in many wineries, some of the phenomena that take place and the parameters that characterize them are barely known. This means that, currently, these wines are still being produced almost empirically. Consequently, to gather information about the intrinsic characteristics of CM wines and to study in depth this winemaking system, it is necessary to carry out small-scale scientific studies. However, it is possible that winemaking in small volumes sometimes does not work in the same way as in industrial cellars and results are not comparable.
This work shows the difficulties and risks of carrying out small-scale winemaking by carbonic maceration and the need to strictly control environmental conditions to achieve it.

2. Materials and Methods

2.1. Assay in Experimental Winery Scale

The study was developed in an experimental winery in 300-L tanks under conditions similar to those in the cellars. In this assay six vinifications were carried out in 300-kg tanks starting from 1800 kg of grapes of the Tempranillo variety. Three tanks were vinified by carbonic maceration (CM) and the other three by destemming and crushing (DC). The chemical composition of the initial must was: probable alcoholic strength 12.8%, pH 3.32, and malic acid 2.49 g/L.
Before the distribution of the bunches into the tanks, 250 kg of grapes were destemmed, crushed, and pressed to obtain 120 L of must that was sulfited at a dose of 40 mg/L of SO2. After this, the CM tanks were filled with industrial CO2 and eventually the whole grape bunches were carefully introduced in a proportion of 270 Kg/tank. Later, a 20-L aliquot of the must obtained previously was added to the upper part of each tank in order to simulate the breakage that occurs in industrial tanks during filling.
AF was developed spontaneously at room temperature and with no pumping over. The carbonic level inside the tanks was checked daily and if necessary, more CO2 gas was added to maintain anaerobiosis. There was also a daily control of the density and temperature of the must taken from the bottom of the tank and the temperature of the bunch mass.
The tanks were devatted when the density of the liquid was 1000, and three fractions from each tank were obtained: free-run liquid in the tank (FCM), liquid after crushing the grapes inside the tank (CCM), and liquid obtained by pressing the solid mass with a pneumatic press (PCM). Subsequently, in each fraction, the alcoholic and malolactic fermentations developed spontaneously. At the end of both processes, the wines were sulfited with 40 mg/L of SO2.
In the vinifications by DC, 270 kg of grapes were destemmed, crushed, sulfited at a dose of 40 mg/L SO2, and placed in each tank. In these processes an additional volume of 20 L of the initial must was also added to equalize volumes. AF took place spontaneously at room temperature. The density and temperature of the liquid was measured daily after pumping over. The vat time was the same as in the tanks made by CM and after devatting and pressing, MLF was occurred spontaneously. In this case, only one type of wine was obtained (DC) as a result of mixing the liquid in the tank with that obtained after pressing the grape skins.

2.2. Physicochemical Analysis

The wines were characterized by measuring the pH, acetaldehyde, and volatile acidity according to the official European Community methods [6]. The pH was measured with a CRISON micropH pHmeter (Barcelona, Spain), the acetaldehyde was determined enzymatically by a Boehringer Manheim test (Darmstadt, Germany), and the volatile acidity was analyzed with a TDI DE2000 distiller/extractor (Barcelona, Spain) and subsequent titration with 0.1 N of NaOH in the presence of phenolphthalein. The malic, lactic, acetic, and pyruvic acids, sugars, and easily assimilable nitrogen (EAN) were determined by enzymatic methods carried out via an automated analyzer (Miura One, TDI, Barcelona, Spain), following the supplier’s instructions.

2.3. Microbiological Analysis

The microbial community present at different times during vinifications (beginning, middle, and end) was analyzed. For this purpose, serial dilutions of the must or wine samples were plated onto different culture media. Total yeasts were measured by seeding onto a GYP culture medium (20 g/L of glucose, 5 g/L of yeast extract, 5 g/L of peptone, and 100 mg/L of chloramphenicol) (Panreac, Barcelona, Spain) and incubation at 28 °C for 48 h. LAB were measured by plating onto an MRS medium (52 g/L of MRS broth, 20 g/L of agar, and 50 mg/L of pymaricine) (Scharlau, Sentmenat, Spain) and incubation at 30 °C under strict anaerobic conditions for at least ten days. Acetic acid bacteria (AAB) were determined by seeding onto a Mann culture medium (25 g/L D-mannitol, 3 g/L peptone, 5 g/L yeast extract, 20 g/L agar, 3 U/mL penicillin and 50 mg/L pymaricine) (Scharlau, Sentmenat, Spain) and incubation at 28 °C for 48 h. Once the plates were seeded and turned over, we added approximately 0.1 g/plate of biphenyl (Merck, Darmstadt, Germany) to the lid to avoid the growth of molds that make it difficult to count colonies. When the incubation periods finished, the plates were examined and colony forming units per milliliter (CFU/mL) were counted in plates with 30–300 colonies.

2.4. Statistical Analysis of the Results

Analysis of variance (ANOVA) was carried out for all the analytical results determined in wines with the IBM® SPSS® Statistic version 23. Significant differences were established by using the Tukey post hoc test (p < 0.05–0.01).

3. Results

3.1. Alcoholic Fermentation during Time in the Vat

The development of the alcoholic fermentation in the free must (FCM) of the CM tanks was slow (Figure 1). The devatting of the tanks occurred after 11 days, when this liquid (FCM) reached a density of 1000. What has been traditionally accepted is that this density is usually reached in less than 8 days [1]. The delay occurred because of a long lag phase of 4 days and because of longer alcoholic fermentations.
Although at the time of devatting and pressing, the DC and FCM wines had almost finished the AF, the CCM and PCM fractions still had a density of 1057, and took another 11 days to finish AF. In winery conditions, the completion of this fermentation is normally achieved in 2–3 days after devatting. In total, the alcoholic fermentation lasted for 14 days in the DC, 15 days in FCM, and 22 days in CCM and PCM.

3.2. Microorganism Development during Time in the Vat

As can be seen in Figure 2A, the yeast population present in CM vinifications was much lower than those of DC. In addition, the level was lower than usual [7,8] because the CM tanks did not reach 5 × 106 colonies/mL, when under normal CM conditions 500 million are exceeded easily. This low number of yeasts could cause a greater development of spoilage bacteria (LAB and AAB) in the CM tanks as can be observed in Figure 2B,C.
As a consequence of the high population of LAB, at the time of devatting, the FCM wine had already started MLF. The contamination of the liquid and the grapes with LAB at this time accelerated the completion of this process in both the FCM and CCM wines (Figure 3). In these two wines there was an overlap of alcoholic and malolactic fermentations and even in CCM wine the MLF ended before the AF, which lasted for 18 and 23 days, respectively. In FCM wines, both fermentations ended at the same time (14 days). However, in PCM wines the degradation of malic acid occurred in two phases (Figure 3), ending 50 days after devatting the tanks.
In the wines made by DC the MLF took place two months after the end of the AF. Therefore, there was no overlap between the two fermentations.
The high LAB populations (Figure 2B) in the liquid phase of the CM tanks probably degraded the sugars and altered the FCM must-wine. There was also a significant development of AAB in the deposits during vatting (Figure 2C).

3.3. Progress of the Intracellular Fermentation (IF)

Table 1 shows the composition of the 3 must-wine fractions obtained at the moment of devatting the CM tanks. Some known effects of the IF on the musts obtained can be seen: high easily assimilable nitrogen (EAN) content [9] and partial degradation of sugars at the time of pressing. A higher amount of acetaldehyde and acetic acid is also observed in musts from whole grapes (CCM and PCM) at the moment of devatting. The acetaldehyde level has higher in PCM while the level of acetic acid was higher in CCM. However, there are no significant differences in pyruvic acid concentration.

3.4. Characteristics of the Wines

As can be seen in Table 2, the most relevant characteristics of the wines obtained were the high levels of volatile acidity and acetaldehyde in the wines made by CM compared to DC ones. In spite of the significant differences found in the pH of wines, there were no great differences between them.
Taking into consideration these results, important deviations were found in the IF in addition to both a lactic and acetic “piqure” produced during the production of CM wines.

4. Discussion

The slow progress of the alcoholic fermentation (Figure 1) was probably due to the low temperature in the tanks. In the CM tanks the temperature of the must never exceeded 22 °C and the average temperature in the clusters throughout the period was 24 °C. In CM vinification, a temperature inside the whole grapes above 30 °C is essential for the IF to proceed optimally [1,2]. In our vinifications the grapes had a temperature of 17 °C when filling the tanks. During the 12 days of fermentation–maceration it was impossible to reach and maintain the optimum temperature (>30 °C). This could be due to the fact that the tanks were of small capacity and made of stainless steel. These characteristics favor the rapid release of the calories generated during fermentation to the environment, and the cooling of the tank (liquid and clusters). The traditional winemakers of the Qualified Designation of Origin (DOCa) Rioja make wines by CM in large capacity tanks made of concrete, a material that has higher thermal inertia than steel. In that case the right temperature is easily reached and maintained, and CM vinification proceeds without problems. But in order to study this vinification system in depth, it is essential to carry out tests with repetitions, and this entails the use of small tanks. In this type of studies, it is therefore necessary to ensure the right temperature to properly conduct the CM vinifications.
In addition, after devatting, CCM and PCM fractions took another 12 days to finish AF. In real winery conditions, the completion of alcoholic fermentation in those wines is normally achieved in 2–3 days, because at devatting time the yeast populations in the tanks are usually very high [2]. These yeasts inoculate the musts obtained after pressing, causing rapid fermentation. The cause that can explain the delay in finishing the AF in CCM and PCM must-wines would be the low yeast population (Figure 2A). For this reason, the yeast population that passed to CCM and PCM wines during crushing and pressing was low, slowing down the end of the alcoholic fermentations.
In addition to the low number of yeasts, a high population of LAB was present in the liquid of the tanks (Figure 2B). Thus, at the devatting moment, the FCM wine had already started MLF and the completion of this process in FCM was fast (Figure 3). During the emptying and pressing, the LAB present in the liquid contaminated the CCM and PCM must-wines, and in some fractions, there was an overlap of alcoholic and malolactic fermentations. This high presence of LAB caused a rapid development of the MLF but also an increase in volatile acidity and even the “piqure” of these wines (Table 2). However, in the wines made by DC the level of BAL was low, there was no overlap between the two fermentations and the volatile acidity level of the wines was correct.
Finally, there was also a great development of AAB in the deposits (Figure 2C). These are strict aerobic microorganisms, and their presence would indicate that, despite the addition of industrial CO2, adequate anaerobiosis was not achieved. Intact berries only shift from oxidative to fermentative metabolism under atmospheres with oxygen content lower than 1% [2]. The morphology of the grape clusters means that air remains trapped in their structure. This air can be difficult to remove just by adding exogenous CO2 to the tank. Perhaps only the continuous supply produced by an intense fermentation of the must at the bottom is capable of eliminating the residual air. This air could favor the development of AAB, which could also contribute to increase the volatile acidity of the wines.
In addition to liquid phase fermentations, IF was taking place inside the whole grape berries. The ability of grapes to adapt to anaerobic atmosphere and initiate IF, even the intensity of this process, depends on different factors that affect the enzymes involved in the process [10]. The conditions that took place in the vinification tanks indicated above could affect the start-up and the development of IF inside the grape berries. The most important reaction of IF within grapes is the metabolism of malic acid that is decarboxylated into pyruvic acid, which is transformed into acetaldehyde, and this finally passes into ethanol [11]. Pyruvic acid can also be transformed into other compounds such as glycerine and acetic, succinic, fumaric, shikimic acids. If the conditions are not suitable for the process, there could be difficulties in the route that could lead to the accumulation inside the grapes of intermediate compounds such as pyruvic, acetaldehyde or acetic acid. The composition of the three must-wine fractions obtained at the moment of devatting from the CM tanks (Table 1), showed a higher amount of acetaldehyde and acetic acid in musts from whole grapes (CCC and PCM). These values could indicate an accumulation of intermediates from the degradation of malic acid during IF. The acetaldehyde level of the different fractions decreases during the subsequent fermentation (Table 2), but the volatile acidity increases probably due to the additional action of the BAL and AAB, which causes abnormally high values of volatile acidity in the final wines.
All the indicated circumstances made the CM wines obtained (Table 2) have high levels of volatile acidity and acetaldehyde. Different studies have shown that carbonic maceration vinification results in wines with slightly higher volatile acidities than destemming [12,13] and high amounts of acetaldehyde [14]. Regarding the acidity parameters, there were no great differences between the wines. A higher pH should be expected in wines from CM [11] due to the degradation of malic acid during IF. However, it is possible that the increase in pH due to this cause was compensated by the high acetic acid content of the three CM fractions.
In conclusion, in this test both lactic and acetic “piqure” occurred during the CM of grapes due to the low development of yeasts and the high populations of bacteria in the vats. There were also deviations in the IF probably because the optimal temperatures and anaerobiosis levels for this process were not reached.

5. Conclusions

In experimental winery scale CM winemaking, there is a risk of spoilage if external methods of temperature control (heating) are not used. This situation is different from when CM wines are made in industrial wineries, where the proper winemaking conditions are easily achieved without applying exogenous heating. The deterioration is caused by the high development of bacteria in the liquid of the tanks during vat and also by a deviation of intracellular fermentation in whole grapes. These results led us to the conclusion that it is necessary to adjust the temperature and the anaerobiosis during the period in vat of the small-scale carbonic maceration vinifications for the correct development of the process.
Until now, it was known that CM wines tend to have higher volatile acidity than those made by DC. The reason that justified this fact was the greater development of LAB during fermentation in the vat and its moderate degradation of the sugars. In this work we have seen that when the conditions in the tanks are not adequate, there is also a greater accumulation of acetic acid inside the grapes which can contribute to increasing the volatile acidity of the wines.

Author Contributions

P.S.: Conceptualization, Data curation, Project administration. L.G.-A.: Investigation, Data curation, Review. R.E.-V.: Investigation. P.G.: Investigation. R.L.: Methodology, Validation, Supervision. S.S.: Data curation, Review. A.R.G.: Conceptualization, Resourcing, Writing—Review and Editing. All authors have read and agreed to the published version of the manuscript.

Funding

This study was co-funded (50/50) by the European Regional Development Fund (ERDF) and the Government of La Rioja, within the ERDF operational program of La Rioja 2014–2020. It was also financed by MCIN/AEI 10.13039/501100011033, Project RTI2018-096051.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Acknowledgments

We would like to thank Ian Thomas for reviewing and correcting the English.

Conflicts of Interest

The authors declare no conflict of interest.

References

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Figure 1. Evolution of the alcoholic fermentation (density) of different types of wines obtained in the experimental winery by destemming and crushing (DC), and in the different fractions obtained in the vinification by carbonic maceration (FCM: free wine, CCM: crushed wine, PCM: press wine).
Figure 1. Evolution of the alcoholic fermentation (density) of different types of wines obtained in the experimental winery by destemming and crushing (DC), and in the different fractions obtained in the vinification by carbonic maceration (FCM: free wine, CCM: crushed wine, PCM: press wine).
Fermentation 08 00027 g001
Figure 2. Evolution of the yeasts (A), lactic bacteria (B), and acetic bacteria (C) populations in the must during the fermentation of wines made by destemming and crushing (DC) and by carbonic maceration (FCM).
Figure 2. Evolution of the yeasts (A), lactic bacteria (B), and acetic bacteria (C) populations in the must during the fermentation of wines made by destemming and crushing (DC) and by carbonic maceration (FCM).
Fermentation 08 00027 g002aFermentation 08 00027 g002b
Figure 3. Evolution of malic acid consumption during vinification in the experimental winery of destemmed and crushed wines (DC) and in the different fractions obtained in the vinification by carbonic maceration (FCM: free wine, CCM: crushed wine, PCM: press wine).
Figure 3. Evolution of malic acid consumption during vinification in the experimental winery of destemmed and crushed wines (DC) and in the different fractions obtained in the vinification by carbonic maceration (FCM: free wine, CCM: crushed wine, PCM: press wine).
Fermentation 08 00027 g003
Table 1. Analysis of the three different fractions obtained at devatting moment of carbonic maceration wines (FCM: free wine, CCM: crushed wine, PCM: press wine). Different letters in the same line mean significant differences between samples (p < 0.05).
Table 1. Analysis of the three different fractions obtained at devatting moment of carbonic maceration wines (FCM: free wine, CCM: crushed wine, PCM: press wine). Different letters in the same line mean significant differences between samples (p < 0.05).
Analytical
Parameters
FCMCCMPCM
Malic acid (g/L)1.09 ± 0.22 a1.85 ± 0.38 b2.17 ± 0.13 b
Lactic acid (g/L)0.78 ± 0.24 b0.33 ± 0.18 a0.22 ± 0.06 a
EAN (mg/L)53.67 ± 8.74 a90.67 ± 5.03 ab133.00 ± 35.59 b
Sugar (g/L)7.98 ± 0.56 a125.9 ± 12.80 b131.0 ± 14.03 b
Acetaldehyde (mg/L)14.39 ± 1.12 a26.79 ± 1.87 b41.70 ± 2.03 c
Pyruvic acid (mg/L)13.64 ± 2.7115.87 ± 3.0217.94 ± 3.91
Acetic acid (mg/L)2.47 ± 0.21 a3.66 ± 0.32 c3.25 ± 0.29 b
Table 2. Chemical composition of the wines vinified by destemming and crushing or by carbonic maceration at the end of alcoholic fermentation. FCM: free carbonic maceration wine, CCM: crushed carbonic maceration wine, PCM: press carbonic maceration wine. Different letters in the same line mean significant differences between samples (p < 0.05).
Table 2. Chemical composition of the wines vinified by destemming and crushing or by carbonic maceration at the end of alcoholic fermentation. FCM: free carbonic maceration wine, CCM: crushed carbonic maceration wine, PCM: press carbonic maceration wine. Different letters in the same line mean significant differences between samples (p < 0.05).
Analytical ParametersDCCarbonic Maceration
FCMCCMPCM
pH3.63 ± 0.02 a3.69 ± 0.04 ab3.70 ± 0.04 ab3.71 ± 0.02 b
Malic acid (g/L)2.36 ± 0.10 c0.07 ± 0.13 a0.02 ± 0.03 a1.17 ± 0.08 b
Lactic acid (g/L)0.22 ± 0.09 a1.39 ± 0.15 b1.26 ± 0.13 b0.53 ± 0.11 a
Volatile acidity (g/L)0.35 ± 0.01 a3.66 ± 0.29 b4.50 ± 0.29 b6.65 ± 0.67 c
Acetaldehyde (mg/L)12.39 ± 0.93 a8.41 ± 0.74 a18.20 ± 1.02 b25.11 ± 1.84 c
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Santamaría, P.; González-Arenzana, L.; Escribano-Viana, R.; Garijo, P.; López, R.; Sanz, S.; Gutiérrez, A.R. Difficulties Associated with Small-Scale Production of Carbonic Maceration Wines. Fermentation 2022, 8, 27. https://doi.org/10.3390/fermentation8010027

AMA Style

Santamaría P, González-Arenzana L, Escribano-Viana R, Garijo P, López R, Sanz S, Gutiérrez AR. Difficulties Associated with Small-Scale Production of Carbonic Maceration Wines. Fermentation. 2022; 8(1):27. https://doi.org/10.3390/fermentation8010027

Chicago/Turabian Style

Santamaría, Pilar, Lucía González-Arenzana, Rocío Escribano-Viana, Patrocinio Garijo, Rosa López, Susana Sanz, and Ana Rosa Gutiérrez. 2022. "Difficulties Associated with Small-Scale Production of Carbonic Maceration Wines" Fermentation 8, no. 1: 27. https://doi.org/10.3390/fermentation8010027

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