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Applied and Environmental Microbiology, February 1999, p. 740-745, Vol. 65, No. 2
0099-2240/99/$04.00+0
Copyright © 1999, American Society for Microbiology. All rights reserved.
Control of Flavor Development in Wine during and
after Malolactic Fermentation by Oenococcus oeni
Jan Clair
Nielsen* and
Marianne
Richelieu
Research and Development, Chr. Hansen A/S,
DK-2970 Hørsholm, Denmark
Received 20 August 1998/Accepted 23 November 1998
 |
ABSTRACT |
During malolactic fermentation in wine by Oenococcus
oeni, the degradation of citric acid was delayed compared to the
degradation of malic acid. The maximum concentration of diacetyl, an
intermediary compound in the citric acid metabolism with a buttery or
nutty flavor, coincided with the exhaustion of malic acid in the wine. The maximum concentration of diacetyl obtained during malolactic fermentation was strongly dependent on the oxygen concentration and the
redox potential of the wine and, to a lesser extent, on the initial
citric acid concentration. The final diacetyl concentration in the wine
was also dependent on the concentration of SO2. Diacetyl combines rather strongly with SO2
(Kf = 7.2 × 103
M
1 in 0.1 M malate buffer [pH 3.5] at 30°C).
The reaction is exothermic and reversible. If the concentration of
SO2 decreases during storage of the wine, the diacetyl
concentration increases again.
 |
INTRODUCTION |
One of the most difficult steps to
control in winemaking is the so-called malolactic fermentation (MLF),
which normally occurs after completion of the alcoholic fermentation.
It is conducted by lactic acid bacteria (LAB), preferably
Oenococcus oeni (formerly known as Leuconostoc
oenos [4]), which deacidify the wine by converting malic acid, a dicarboxylic acid, to lactic acid, a monocarboxylic acid, resulting in a wine with a softer mouth feel. In
addition, the MLF also affects the final aroma and taste balance by
modifying fruit-derived aromas and producing aroma-active compounds (8).
In recent years, the introduction of commercial freeze-dried bacterial
cultures of O. oeni for direct inoculation into wine has
improved the control of MLF (17). Commercial cultures ensure better control of the time of onset and the rate of MLF, reduce the
potential for spoilage by other bacteria, and reduce potential interference by bacteriophages (6). The winemaker can now
pay more attention to the control of the flavor modifications induced by O. oeni.
Not only malic acid but also citric acid in the wine is metabolized by
O. oeni (Fig. 1). One of the
intermediary compounds in the metabolism of citric acid is diacetyl,
which is considered one of the most important flavors produced during
MLF (8, 21). When present at a concentration above the
sensory threshold, diacetyl gives the wine an aroma which can be
characterized as buttery or nutty. It has been demonstrated that
threshold values in different wines vary from 0.2 mg/liter in
Chardonnay wine to 0.9 mg/liter in Pinot Noir and 2.8 mg/liter in
Cabernet Sauvignon wine (11). The source of diacetyl is
-acetolactic acid (ALA), an unstable compound that besides the
enzymatic decarboxylation by the bacteria also may decarboxylate
spontaneously to acetoin and, in oxidizing conditions, also to
diacetyl. In LAB-fermented dairy products, the latter reaction is now
generally believed to be the only source of diacetyl (7).
Diacetyl is reduced further by O. oeni to acetoin and
2,3-butanediol, which in normal concentrations has no influence on the
wine aroma (18).
Understanding the factors influencing the diacetyl concentration is
critical for the control of the final flavor in wine. The objective of
this paper is to describe the dynamics of the citrate metabolism during
MLF by O. oeni and how the concentration of the intermediary
compound, diacetyl, is influenced by different physicochemical factors.
 |
MATERIALS AND METHODS |
Wine.
The wine used in the experiments was prepared from
Chardonnay grape juice which was ultrahigh temperature treated (120°C
for 10 s) just after the pressing. The juice was inoculated with
Saccharomyces cerevisiae (Saint-George S101, Fould-Springer,
France), and the alcoholic fermentation was conducted at 20°C in
5-liter glass containers fitted with fermentation locks. After the
alcoholic fermentation, the yeast was removed from the wine by being
filtered through a 0.45-µm-pore-size filter (Sartobran capsule from
Sartorius). After filtration, the wine data were as follows: 12.0%
(vol/vol) ethanol, 2.4 g of L-malic acid per liter,
0.35 g of citric acid per liter, and pH 3.4. The MLF in the wine
was initiated by direct inoculation with freeze-dried O. oeni (Viniflora oenos; Chr. Hansen) to a concentration of 5 × 106 CFU/ml. Unless stated otherwise, all handling of the
wine was conducted without access by atmospheric air by flushing
bottles, filters, tubes, etc., with N2.
Experimental conditions.
The experiments with MLF under
anaerobic and semiaerobic conditions were conducted in 2-liter
wide-mouth bottles (Schott Glaswerke, Mainz, Germany). The semiaerobic
conditions were obtained by placing a loose plastic lid on the bottles,
leaving access by air to the wine while the anaerobic conditions were
maintained by use of rubber stoppers on the bottles. Redox potential
and O2 concentration were measured by continuously pumping
wine from the bottles into a small container equipped with a redox and
O2 electrode until the readings from the electrodes were
constant. The wine removed from the anaerobic bottles during the
measurements was replaced by N2.
The wine with completed MLF used in the physicochemical experiments was
filtered through a 0.45-µm-pore-size filter (Sartobran
capsule from
Sartorius) before use in order to remove the bacteria.
Wine storage
experiments were conducted in 2-liter wide-mouth
bottles fitted with
rubber stoppers and fermentation
locks.
The SO
2 added to the wine was from a 10,000-mg/liter stock
solution prepared from K
2S
2O
5, and
the diacetyl added was from
a 5,000-mg/liter stock solution. All
experiments were conducted
at 20°C.
Bacterial enumeration.
The enumeration of viable bacteria
was performed after appropriate dilution in water containing 0.1%
peptone and 0.9% NaCl, followed by pour plate seeding in MRS agar
(Oxoid Ltd.) with pH 5.0. Viable counts were obtained as the number of
CFU after incubation at 30°C for 7 days.
Physicochemical analyses.
The redox potential and the
O2 concentration were measured respectively with a
combination platinum electrode (Pt 4865-50-SC-S7) with the Xerolyt
Ag:AgCl reference system and with an O2 electrode (inst.
type: MO 128) calibrated in wine at 0% O2 with
N2, and then at 21% O2 with air (both
electrodes from Mettler Toledo, Urdorf, Switzerland). Wine samples for
analyses were stored at
20°C until analyzed. L-Malic
acid, citric acid, and acetic acid were determined by the enzymatic
test kits of Boehringer Mannheim. Ethanol and total SO2
were determined according to the method of Schmitt (23).
Diacetyl, ALA, and acetoin were determined by headspace gas
chromatography as described by Richelieu et al. (
22), except
for the fact that the oven temperature was held at 60°C for 2
min,
the total cycle time was 20 min, and the sample temperature
for
diacetyl was 30°C.
The two isomer forms of acetoin and three isomer forms of
2,3-butanediol were determined by gas chromatography. The gas
chromatograph
(HP 5890, Hewlett-Packard, Palo Alto, Calif.) was
equipped with
a mass selective detector (HP 5972; Hewlett-Packard) with
a 25-m
fused silica capillary column (0.25-mm inside diameter, CP
Chirasil-Dex
coating; part no 7502; Chrompack International BV, 4330 EA
Middelburg,
The Netherlands). The gas chromatograph was connected to a
Hewlett-Packard
autosampler (model HP 7673A). The operating parameters
of the
gas chromatograph were as follows: 1.0-µl samples injected in
a split ratio of 1:30, 25 KPa of head pressure, 21-ml/min helium
as
carrier gas, and 250°C injector and detector temperatures.
The oven
temperature was held at 60°C for 3 min; the temperature
was then
increased in increments of 20°C/min up to 220°C, which
was held for
5 min. To avoid any possible systematic effects on
the final results,
all samples for gas chromatography were randomized
prior to analysis.
The total 2,3-butanediol concentration was
calculated from the sum of
the three isomer
forms.
All experiments were conducted in duplicate. Unless stated otherwise,
the chemicals used were of analytical
grade.
 |
RESULTS |
Figure 2 shows the MLF and the
dynamics of the citrate fermentation induced in wine by direct
inoculation with freeze-dried O. oeni. There was no loss of
viability after inoculation, and the bacteria started to grow after 4 days and completed the degradation of malic acid in 8 days. The
bacteria also degraded the citric acid. However, this degradation was
delayed for several days compared to the degradation of the malic acid.
The concentration of ALA increased during the catabolism of citric
acid, and maximum was obtained just before the exhaustion of the citric
acid. The concentration of diacetyl followed the same pattern,
resulting in a maximum concentration just after completion of the MLF.
ALA and diacetyl were further degraded by the bacteria to acetoin (Fig.
2). Both R and S isomers of acetoin were
measured, although it was not possible to identify which was the
R and which was the S form. One of the isomers
dominated in the first part of the citric acid metabolism, and the
other dominated toward the end (results not shown). This fluctuation
probably reflects different formation pathways which may be by diacetyl
reductase and ALA decarboxylase of the bacteria and by chemical
decarboxylation of ALA. Acetoin was further reduced to 2,3-butanediol
by the bacteria, about 80% of it as the mesoisomer.

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FIG. 2.
The dynamics of the citrate fermentation during MLF in
Chardonnay wine. The MLF was initiated by direct inoculation of
freeze-dried O. oeni and conducted under anaerobic
conditions.
|
|
In practice, the physicochemical parameters for the MLF, including the
redox potential and oxygen concentration, vary according to the local
and individual vinification techniques. To examine in more detail the
influence of the oxygen concentration and redox potential, MLF was
conducted under anaerobic and semiaerobic conditions (Fig.
3). Under the anaerobic conditions, the
redox potential decreased below 150 mV when the bacteria started to
grow, and the oxygen concentration was less than 0.2 mg/liter
throughout the fermentation. In the semiaerobic fermentation, the redox
potential stabilized above 300 mV and the oxygen concentration
stabilized between 2 and 4 mg/liter. The results in Fig. 3 show that
the two different fermentation conditions had no influence on the degradation of malic and citric acid by the bacteria and that the
growth of the bacteria during the degradation was almost the same in
both fermentation conditions. However, large differences were observed
for the diacetyl and acetoin concentrations. Under semiaerobic
conditions, the diacetyl concentration reached 13 mg/liter, which was
considerably higher than the 2 mg/liter obtained under anaerobic
conditions. The acetoin concentrations showed the opposite behavior. A
maximum of 20 mg/liter was obtained under anaerobic conditions, and 12 mg/liter was obtained under semiaerobic conditions. After exhaustion of
malic and citric acid from the wine, the bacteria in the semiaerobic
wine continued to grow, while the anaerobic wine did not support any
further growth.

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FIG. 3.
The effect of anaerobic and semiaerobic conditions on
the citrate fermentation during MLF in Chardonnay wine. The MLF was
initiated by direct inoculation of freeze-dried O. oeni.
|
|
The same fermentations were conducted with addition of 1 g of
citric acid per liter to the wine (Fig.
4). The redox potentials and oxygen
concentrations showed the same pattern as in the fermentations without
citric acid addition. Likewise, the bacterial population and
degradation of malic and citric acid were again very similar under both
the anaerobic and the semiaerobic conditions. The results clearly
confirm that the degradation of citric acid is delayed compared to the
degradation of malic acid. The extra citric acid had a pronounced
effect on the diacetyl and acetoin concentrations. Under semiaerobic
conditions, the diacetyl concentration reached a maximum of 29 mg/liter, more than twice the concentration obtained without addition
of citric acid (Fig. 3). Under anaerobic conditions, the extra citric
acid did not result in an increased diacetyl production. The maximum
concentration of 2 mg/liter was similar to that for the wine without
addition (Fig. 3 and 4). The maximum acetoin concentration obtained
under semiaerobic conditions was not affected by citric acid addition
(Fig. 3 and 4). However, under anaerobic conditions, the citric acid
addition resulted in an increase in the maximum concentration of
acetoin from 20 mg/liter (Fig. 3) to 75 mg/liter (Fig. 4). Figures 2,
3, and 4 show that O. oeni very effectively reduced both the
diacetyl and the acetoin concentrations in the wine once the citric
acid had been exhausted.

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FIG. 4.
The effect of anaerobic and semiaerobic conditions on
the citrate fermentation during MLF in Chardonnay wine supplemented
with 1 g of citric acid per liter. The MLF was initiated by direct
inoculation of freeze-dried O. oeni.
|
|
Besides the microbial activity, the final diacetyl concentration in
wine is also affected by the concentration of SO2. The main
sources of SO2 in wine are from the addition to the grape juice before the alcoholic fermentation, from SO2 produced
by the yeast during the alcoholic fermentation, and from the addition after completion of the MLF. The last-mentioned addition, which normally stops all further microbiological activity, is the largest. SO2, which exists predominantly as the bisulfite ion at the
pH observed in wine, has the ability to react with many different compounds in the wine, including carbonyl compounds like diacetyl (2). Generally, the reaction of SO2 with
carbonyl compounds can be written as shown in Fig.
5.
The reaction, which is reversible, is very important for the diacetyl
concentration in wine. The formation equilibrium constant, Kf, of the reaction at different temperatures
was calculated from headspace gas chromatography determinations of the
diacetyl concentration in 0.1 M malate buffer (pH 3.5) to which were
added variable concentrations of diacetyl and SO2. At 30, 45, and 70°C, the Kfs were calculated to be 7.2 × 103, 2.2 × 103, and
0.6 × 103 M
1, respectively, indicating
that the reaction is exothermic, i.e., the equilibrium moves to the
left with increasing temperatures. For practical illustration, Fig.
6 shows the diacetyl concentrations measured in wine with completed MLF and different amounts of
SO2 and diacetyl added. The measured diacetyl
concentrations are somewhat higher than those expected from the
Kf determined in the malate buffer. Most
probably this is because SO2 also reacts with compounds other than diacetyl in the wine. Nonetheless, Fig. 6 illustrates how
SO2 rather effectively reduces the diacetyl concentration in a wine with completed MLF. For instance, addition of 80 mg of
SO2 per liter, which is within the range used in the wine
industry, reduced the diacetyl concentration from initially 20 to 5 mg/liter, i.e., by 75%.

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FIG. 6.
The diacetyl concentration measured in Chardonnay wine
with completed MLF and addition initially of the following: 20 mg of
diacetyl per liter and different amounts of SO2 ( ) or 80 mg of SO2 per liter and different amounts of diacetyl
( ).
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|
Figure 7 shows the influence of pH on the
diacetyl concentration in wine to which were added initially 20 mg of
diacetyl/liter and 80 mg of SO2/liter. The influence was
determined both before and after MLF in the wine. The results show that
the pH has only a weak influence on the reaction between diacetyl and
SO2 in the pH range of 4.0 to 2.6, which covers most wines.
What is more important for the diacetyl concentration is whether the
wine has been taken through the MLF. In the wine without MLF, the
diacetyl concentrations were about twice the concentrations measured in the wine with MLF.

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FIG. 7.
The effect of pH in Chardonnay wine on the diacetyl
concentration measured after addition of 20 mg of diacetyl per liter
and 80 mg of SO2 per liter. The effect was examined in the
wine before MLF ( MLF) and after MLF (+MLF).
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|
After sulfitation, most wines are stored in tanks, barrels, or bottles
in a span ranging from a few months to several years. During this
storage, some of the SO2 will evaporate and some will react, reversibly or irreversibly, with different compounds in the
wine, including oxygen diffusing into the wine from the surroundings. This affects the diacetyl concentration in the wine because of the
reversible nature of the reaction between diacetyl and SO2. Figure 8 shows results of an accelerated
storage experiment where wine with diacetyl and different
concentrations of SO2 added was stored in 2-liter glass
bottles fitted with rubber stoppers and fermentation locks. The results
show that immediately after the addition some of the SO2
combined with part of the diacetyl. However, during the 4 weeks of the
experiment, the total SO2 concentration, i.e., the sum of
uncombined and reversibly combined SO2, was reduced in all
bottles and at the same time a concomitant increase in the diacetyl
concentration in the wines was observed. It was beyond the scope of our
work to identify the fate of the missing SO2 during the
experiment.

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FIG. 8.
The effect of storage time on the diacetyl and total
SO2 concentrations in Chardonnay wine with completed MLF
and initial addition of 20 mg of diacetyl per liter and different
amounts of SO2. conc., concentration.
|
|
 |
DISCUSSION |
The catabolism of malic and citric acid in the wine by O. oeni was not concomitant but sequential. The observations seem to be very consistent because similar results have been obtained with
different strains of O. oeni in wines from different parts of the world (16, 18). It is likely that the presence of
malic acid inhibits the activity of one or more of the enzymes in
the citric acid metabolism of the bacteria. Martineau and Henick-Kling (12) found that the presence of malic acid in the culture
medium inhibited citric acid transport, and Lonvaud-Funel et al.
(9) found that the activity of citrate lyase was maximal
after the malic acid had disappeared. At many wineries, the exhaustion
of malic acid in the wine is used as the criterion for completion of the MLF and thereby for the time of sulfitation, which stops all
further microbiological activity. Our results show that this criterion
may result in an incomplete citric acid degradation in the wine.
The concentration of ALA measured in wine was very low compared to the
concentration normally observed in dairy products fermented with
citrate-fermenting LAB, and only a new sensitive detection method
(22) made the determination in wine possible. There may be
several reasons for the low concentration. Ramos et al. (20) found that the ALA decarboxylase level in O. oeni is 10 times higher than the ALA synthetase level. Besides, ALA is an unstable compound that may decarboxylate spontaneously to either diacetyl or
acetoin, especially at a low pH such as the pH in wine (14, 22).
Fluctuations in the diacetyl concentration caused by O. oeni
have been reported by several persons (3, 19). In accordance with our previous observations (16), the maximum diacetyl
concentration was obtained around the time when malic acid was
exhausted from the wine followed by degradation again by the bacteria.
For control of the final diacetyl concentration in the wine, it is
important to be aware of this coincidence of maximum diacetyl
concentration and exhaustion of malic acid. If the wine is sulfited at
this point, which is common at many wineries, all further
microbiological activity stops. And so does the irreversible reduction
of the diacetyl, because this can be accomplished only by living
bacteria and yeast (16). If the buttery note from diacetyl
is too overwhelming after exhaustion of the malic acid, it is advisable
to hesitate with sulfitation until the diacetyl concentration has been
reduced by the bacteria and yeast.
The total production of diacetyl and acetoin during the MLF by O. oeni was stimulated by increased citric acid concentrations in the
wine. However, the production of the two compounds was not equally but
strongly dependent on the redox potential and O2
concentration of the wine. Similar results have been reported for skim
milk fermented with the ALA-accumulating strain of Lactococcus lactis subsp. lactis biovar diacetylactis
(15). An examination of synthetic ALA shows that the
spontaneous decarboxylation of ALA to diacetyl is strongly favored by
high redox potential and O2 concentration and low pH, such
as the pH in wine (14, 22). From this and the fact that
diacetyl synthetase has never been isolated from LAB, it seems most
likely that the diacetyl in wine is the result of a pure chemical
reaction between ALA and O2. At low redox potentials and
O2 concentrations, the ALA is converted almost exclusively,
either chemically or by the bacterial ALA decarboxylase, to acetoin.
After the malic and citric acids were degraded, the bacteria in the
semiaerobic wine continued to grow in contrast to the bacteria in the
anaerobic wine. It is possible that certain compounds in the wine can
function as a substrate for O. oeni only when O2
is available. Certain substrates, such as polyols, have been reported
to be fermented by some LAB only when O2 is available (1, 5).
Sulfite added to wine reacts fast and rather strongly with diacetyl and
thereby reduces the buttery flavor. However, in contrast to the
microbiological reduction by bacteria and yeast, this reaction is
reversible. If some of the SO2 evaporates or combines with other compounds in the wine, the concentration of the flavor may later
increase in the wine again. This should be kept in mind when the time
of sulfitation after the MLF is decided and when the wine is stored in
tanks or barrels and later bottled.
The concentration of free diacetyl in wine containing SO2
may also depend on the concentration of other SO2-binding
compounds, such as acetaldehyde,
-ketoglutaric acid, and pyruvic
acid. Mayer et al. (13) found that these compounds are
substantially reduced during MLF. Accordingly, we measured a decrease
in the concentration of acetaldehyde, which combines very strongly with
SO2 (Kf = 7 × 105
M
1 [2]), from initially 17 mg/liter
to 1.5 mg/liter at the end of the MLF. The proportion of
SO2 available for reaction with diacetyl is therefore
higher in wine after the MLF than before, and this probably explains
the observed lower proportion of free diacetyl in wine after the MLF
than before (Fig. 7).
Several publications have described the influence of the diacetyl
concentration on the wine flavor (11, 21). The present results show that if the wine contains SO2, it is important
to be aware of the reversible and exothermic reaction of
SO2 with diacetyl when the actual diacetyl concentration in
the wine is determined and correlated with an organoleptic evaluation.
If, e.g., headspace gas chromatography is used for the determination, as in this publication, the sample equilibration temperature should not
be higher than 30°C in order not to overestimate the actual diacetyl
concentration. The exothermic nature of the reaction also indicates
that if one wishes to accentuate the buttery-nutty aroma of diacetyl
in, e.g., a bottle of Chardonnay, it should be consumed at 20 rather
than at 10°C.
 |
FOOTNOTES |
*
Corresponding author. Mailing address: Research
and Development, Chr. Hansen A/S, Boege Allé 10-12, DK-2970
Hørsholm, Denmark. Phone: 45 45747474. Fax: 45 45748994. E-mail:
jcn.dk{at}chr-hansen.com.
 |
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0099-2240/99/$04.00+0
Copyright © 1999, American Society for Microbiology. All rights reserved.
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