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Changes in Organic Acids During Malolactic Fermentation pp.191-195 Volume 105 No. 3,1999
Changes in Organic Acids During Malolactic Fermentation
at Different Temperatures in Yeast-Fermented Apple Juice
by Monica Herrero, Isabel Cuesta, Luis A. Garcia and Mario Diaz
Department of Chemical Engineering and Environmental Technology, University o/Oviedo, Spain
Received 23rd October 1998
Organic acids were analyzed during controlled malolacticfermentation conducted by a selected
Leuconostoc oenos strain, performed at different temperatures (15 °C, 22 °C and 27 °CX The apple
juice had been previously fermented by a Saccharomyces cerevisiae strain, at 15'C and major
organic acids were also monitored during this phase. The aim of this work was to study the
effect offermentation temperature on organic acid composition and on the main reactions that
take place during malolacticfermentation, applicable to improving the cider making process at
the industrial level.
Key Words: Apple juice, organic acids, high performance liquid chromatography,
fermentation.
malolactic
INTRODUCTION
Organic acid composition in alcoholic beverages, and in
cider in particular, is a very important feature that
affects the organoleptic properties of the product. Being
a constituent of the sourness group, each acid in
alcoholic beverages conveys a characteristic flavour,
aroma or taste. During malolactic fermentation, lactic
acid bacteria transform malic acid into lactic acid, thus
reducing the excessively high acidity found in apple
juice. Malolactic conversion is also accompanied by
formation of products other than lactic acid, modifying
both flavour and texture.3-8-4 Malolactic fermentation can
remove strong vegetative/herbaceous aromas, enhance
fruity and floral aromas, improve the mouthfeel and
extend the duration of the aftertaste. Not only
composition, but also concentration, of each acid is
essential in the quality of the product. Concentration
threshold values and the relative sourness of the most
important non-volatile acids in cider have been
previously reported15.
When malolactic fermentation occurs spontaneously,
the flavour characteristics are unpredictable due to
the different microorganisms which may be present in
the must or in the cellar. The use of starter cultures in
wine and cider making ensures achievement of
malolactic fermentation in a more rapid and
predictable manner, and also provides uniformity to
the final product.
Technological parameters also affect the odour and
taste of cider. For example, fermentation temperature
strongly affects the development of malolactic
fermentation and lactic acid bacteria metabolism10. The
aim of this work was to determine the main changes in
organic acids that take place during malolactic
fermentation, conducted at different temperatures. A
selected malolactic indigenous strain was used as starter
culture, in diluted concentrated apple juice previously
fermented by a selected yeast strain. This study, at the
laboratory level, was carried out with the goal of
determining the optimal conditions to perform a
controlled malolactic fermentation in cider production.
MATERIALS AND METHODS
Microorganisms
A commercial active-dried yeast strain of
Saccharomyces cerevisiae was used. The malolactic
bacteria (strain Lc2) was previously isolated in the cellar
of the cider industry Escanciador, S.A. (Villaviciosa,
Asturias, Spain), and was identified as Leuconostoc oenos.
It was selected on the basis of its ability to perform malic
acid degradation.
Experimental conditions
Concentrated apple juice, supplied by an industrial
cider factory, was reconstituted with distilled water
(1:6), yielding a final density of aprox. 1060 g/litre. The
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Volume 105, No. 3,1999 Changes in Organic Acids During Malolactic Fermentation
juice was sterilized in a tangential flow filtration device
(Filtron Omegacell 150™) connected to a peristaltic
pump, using polyethersulfone membranes (0.33/<m pore
diameter).
Fermentations were carried out in pre-sterilized 250
ml Erlenmeyer flasks containing 100 ml of the culture
medium which were placed in an orbital shaker (New
Brunswick, G25) at 100 r.p.m, at the assay temperatures.
Yeast active-dried preparation was rehydrated in
sterile apple juice and grown under aerobic conditions
at 250 r.p.m., 28°C, for 18 h. The apple juice was then
inoculated with yeast at a final concentration of 106
cfu/ml. Alcoholic fermentation by yeasts was carried
out at 15"C.
Once the alcoholic fermentation was completed and the
density reached approximately 1005 g/litre, a high bacterial
inoculum (107 cfu/ml) was added to the flasks to start
malolactic transformation. The samples were incubated at
the assay temperatures, under the same conditions.
Malolactic bacteria was previously grown in apple juice,
prepared as described above, supplemented with yeast
extract 0.5% (w/v) and statically incubated at 30°C, due to
the microaerophilic nature of this bacteria. Incubation was
for 6 days until the stationary phase was reached.
Sample preparation and analytical methods
Apple juice and cider samples were filtered through
0.45 /*m membranes. Medium density was mesured by
picnometry. L-malic, D- and L-lactic acid were
determined by enzymatic assays (Boehringer
Mannheim). Organic acids in samples were determined
by HPLC (Waters, Alliance 2690), equipped with a
photodiode array detector (Waters 996), as previously
described7-'. A Spherisorb ODS2 (C18) analytical column
(4.6 x 150mm, 3/<m, Waters) was used under the
following conditions: column temperature, 36°C; mobile
phase, 10-2 m KH2PO4/H3PO4 pH 2.65; flow rate, 0.5
ml/min, and 10/<l volume injection. Column effluents
were monitored at 210 nm. Solvents were HPLC grade.
Analytical grade organic acids (without further
purification) were used as standards: quinic, pyruvic,
malic, shikimic, lactic, acetic, fumaric and succinic acids
were purchased from Sigma-Aldrich and Merck.
Quantification was based on peak area measurements.
Data treatment was performed with Millenium software
(v.2.15.01).
RESULTS AND DISCUSSION
Apple juice was initially fermented by the selected
yeast strain at 15°C. Once the alcoholic fermentation was
completed, the inoculum of malolactic bacteria was
added to the flasks (107 cfu/ml) and further incubation
was performed at 15*C, 22°C and 27°C under the same
conditions.
Some aspects may be highlighted about the alcoholic
fermentation by yeast at 15°C. Pyruvic acid reached a
maximum when approximately half the sugar has been
fermented (Fig. 1). This acid is an intermediate in the
Embden-Meyerhof-Parnas pathway and a precursor to
many other substances. In spite of its importance as a
MLF
FIG. 1. Pyruvic acid evolution during alcoholic
fermentation (AF) by S. cerevisiae at 15°C, and during
malolactic fermentation (MLF) by L. oenos at 15°C (■),
22°C (•) and 27'C (A).
metabolic intermediate, it is excreted by yeast during
fermentation, sometimes in concentrations ranging in
cider from 0.08 to 0.6 g/litre.14 As it is shown in Figure 2,
the strain of S. cerevisiae used in this work was able to
consume malic acid. Yeasts may either break down or
form malate during fermentations. They convert malate
to ethanol and CO2 anaerobically via the malic enzyme.
In a survey of 300 strains of Saccharomyces using
synthetic medium, the proportion of malate degraded
MLF
FIG. 2. L-Malic acid during AF (15°C) and MLF (15°C
(■), 22°C (•) and 27'C (A)).
192 Journal of The Institute of Brewing
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Changes in Organic Acids During Malolactic Fermentation Volume 105 No. 3,1999
MLF MLF
35 40
10 15 20 25 30 35
FIG. 3. D-lactic acid (open symbols) and L-lactic acid
(solid symbols) during AF (15°C) and MLF at the three FIG. 6. Fumaric acid during AF (15°C) and MLF at 15°C
temperatures tested: 15°C (■), 22°C (•) and 27°C (A). (■), 22°C (•) and 27°C (A).
MLF
15 20 25 30 35 40
FIG. 4. Production of acetic acid during alcoholic
fermentation (AF) at 15'C and malolactic fermentation
(MLF) at 15°C (■), 22°C (•) and 27"C (A).
MLF
0 15 20 25 30 35 40
CO
FIG. 5. Succinic acid production at 15°C (■), 22'C (•)
and 27°C (A) during MLF and AF at 15°C.
for each strain varied from 5 to 40%.u Production of L-
lactate was detected (Fig. 3). Reduction of pyruvate may
result in formation of either D(-)- or L(+)- lactate.14
In addition, formation of acetic (Fig. 4), succinic (Fig. 5)
and fumaric (Fig.6) acids were observed. The later
showed a maximum in the first stages of alcoholic
fermentation.
Once malolactic bacteria were inoculated in the
fermentation media, L-malic acid was rapidly consumed
and as shown in Figure 2, this process was significantly
affected by temperature. At 15°C, the rate of
consumption of malic acid was slower than at higher
temperatures (22°C and 27°C). Based on this result, 22°C
should be selected as the optimal temperature for malic
acid degradation, since at 27*C residual malic acid was
detected until 32 days. Previously published results
have determined that the optimal temperature for
malolactic fermentation in wine production was 20-
25°C.6 It should be pointed out that the amount of L-
lactic acid formed (Fig. 3) did not correspond to the
amount of L-malic acid consumed under all
temperatures assayed. This fact could be explained by
taking into account the fact that yeast metabolism could
be responsible for part of malic acid degradation
occurring during this phase. However, two additional
features were detected at the three fermentation
temperatures tested. An interesting decrease in L-lactic
acid was observed, being higher at 27°C than at 15°C. It
has been reported in the literature that lactic acid
bacteria have the ability to oxidize lactic acid to acetate
anaerobically.13 Both D- and L-lactate are equally good
hydrogen donors for the reductive steps and
simultaneously lactate is oxidized to acetate. In
addition, some strains of Leuconostoc isolated from
ciders and perries produced appreciable amounts of
succinate from malate,2 the proportion varying with the
particulate isolate and increasing with the pH of the
medium. This reaction is known as "malosuccinic
Journal of The Institute of Brewing 193
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Volume 105, No. 3,1999 Changes in Organic Acids During Malolactic Fermentation
fermentation". Succinic acid production was observed at
the three fermentation temperatures (Fig. 5) with the
greatest concentration being reached at 27*C and 15°C
The concentration of sucdnic add at these temperatures
was inversely related to the levels of L-lactic add
measured. Some yeasts are also capable of converting
some malate to succinate and smaller amounts of
lactate,14 which was demonstrated using 14C-labelled
malate. Previous work9 regarding Spanish cider
manufacture (from the Asturian region) reported similar
results: an L-lactic add decrease with time during
malolactic fermentation and the amount of L-lactic add
formed was less than the theoretical value expected
from the malic acid conversion.
A second major organic add present in apple juice,
together with malic add, is quinic add. Some Leuconostoc
strains reduce quinate and the related shikimate,13 which
is a minor component in apple juice. Quinic add is
reduced to dihydroshikimic add after the completion of
malolactic fermentation. Its esters, chlorogenic add and
p-coumarylquinic acid, are usually reduced at a later
stage of fermentation. Shikimic add, is coupled to a
major redox system (shikimate /dihydroshikimate) in
the metabolic action of lactic add bacteria, involving the
oxidation of substrates such as fructose and lactic
acid.11-12 The concentrations of quinate (Fig. 7) showed
significant differences between 15°C and the higher
fermentation temperatures of 22°C and 27°C, where this
add was not detected from days 25 and 19, respectively.
4
3.5
3
2.5
2
1.5
1
0.5
n
AF
Ti—
•
■
MLF
%
\%«
\V
>•
10 15 20 25
Days
30 35 40
FIG. 7. Quinic add. The symbols represent the same
conditions.
Quinic acid metabolism is related to malic acid
consumption and is involved in anaerobic lactate
oxidation mechanisms. Consumption of shikimic add
was also monitored and was metabolized earlier at
higher fermentation temperatures (Fig. 8).
The formation of pyruvic add was also affected by the
fermentation temperature. At higher temperatures,
0.004
0.0035
0.003
*& 0.0025
I 0.002
| 0.0015
0.001
0.0005
0
AF MLF
■■ ■
MM MM *
0 5 10 15 20 25 30 35 40
Days
FIG. 8. Shikimic add. The symbols represent the same
temperatures.
increasing maximum levels were reached in succesive
later stages of fermentation (Fig. 1). It has been
postulated that lactic add may be oxidized to acetate
and CO2 by lactic add bacteria, with pyruvate as an
intermediate product.5 These maximum levels of
pyruvate during malolactic fermentation could be
related to this reaction.
Fumaric acid formation reached a maximum at the
beginning of the malolactic transformation, and then
decreased in a similar way as malic add degradation at
each fermentation temperature. Once malic add was
fully metabolized, a second increase was detected, at
15'C and 22*C.
The rate of acetic add formation during the first
stages of malolactic fermentation (Fig. 4) was greatest at
the highest temperature tested. No significant
differences were observed for acetic add formation
between 15°C and 22*C, both reaching a maximum level
of 0.8 g/litre. From day 20 until the end of the
fermentation process, an important increase in the rate
of production of acetic acid was observed at all
temperatures assayed, reaching concentrations of
lg/litre at 15°C, and higher concentrations at 22°C and
27°C. These concentrations of acetic acid would
negatively affect the organoleptic properties of the
product. In all experiments, fermentation conditions
were mantained for 40 days, although malic acid was
consumed earlier in all cases. Acetic acid production at
the later stages can be directly related to the oxidation
mechanisms of lactate metabolism (involving quinate
and dihydroshikimate, or pyruvate as intermediate)
both giving rise to acetate as the final product. In cider
production, malic acid consumption usually indicates
the end of the fermentation process, avoiding further
acetic acid formation.
194 Journal of The Institute of Brewing
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Changes in Organic Acids During Malolactic Fermentation Volume 105 No. 3,1999
CONCLUSIONS
Fermentation temperatures during malolactic
transformation significantly affect the concentration
levels of the major organic acids in cider. Regarding the
malic acid consumption rate, 22°C turns out to be the
most favourable temperature. Based on these results , it
has been postulated that in all experiments carried out,
a parallel malosuccinic fermentation may be occurring
in addition to the malolactic fermentation. An important
decrease in L-lactic acid was observed at each
temperature tested, once malic acid had been degraded.
This can be explained by anaerobic lactate oxidation
mechanisms from the action of malolactic bacteria.
Consumption of quinate and shikimate and formation of
pyruvate as an intermediate product have been
measured, producing acetate as a final product at the
later stages of the fermentation process. To avoid
elevated concentrations of acetic acid in the product,
fermentation temperatures between 15°C and 22°C
seems to be more suitable than 27°C.
Acknowledgements. This work was financially
supported by the following Asturian cider industries:
Sidra Escanciador, S.A., Valle, Ballina y Fernandez, S.A.,
Sidra Mayador, S.A. and Industrias Zarracina, S.A.
(Asturias, Spain) and by FICYT (Foundation for
Scientific and Technical Research, Asturias, Spain).
REFERENCES
1. Blanco, D., Moran, M.J., Gutierrez, M.D. and Mangas, J.J.
Chromatographia, 1988, 25, 1054-1058.
2. Carr, J.G. and Whiting, G.C. Reports of Long Ashton Research Station
for 1955,1956, 163-168.
3. Davis, C.R., Wibowo, D., Eschenbruch, R., Lee, T.H. and Fleet, G.H.
American Journal of Etiology and Viticulture, 1985, 36, 290-301.
4. Henick-Kling, T. Wine microbiology and biotechnology, Ed. G.T. Fleet,
Chur, Harwood Academic Publishers, 1993, 289-326.
5. Kandler, O. Antonic van Leeuwenhoek, 1983, 49, 209-224.
6. Lafon-Lafourcade, S. Biotechnology. Vol. 5, Ed. G. Reed, Heidelberg,
Verlag-Chemie, 1983, 81-163.
7. Mangas, J. J. PhD thesis. Department of Analytical Chemistry.
University of Oviedo.
8. Salih, A.G., Drilleau, J.F., Cavin, J.F., Divies, C. and Bourgeois, CM.
journal of the Institute of Brewing, 1988, 94, 5-8.
9. Salih, A.G., Le Quere, J-M-. and Drilleau, J-F. Journal of the Institute
of Brewing, 1990, 96, 369-372.
10. Vaillant, H., Formisyn, P. and Gerbaux, V. Journal of Applied
Bacteriology, 1995, 79, 640-650.
11. Whiting, G.C. and Coggins, R.A. Biochemical Journal, 1969,115,60-61.
12. Whiting, G.C. and Coggins, R.A. Antonie van Leeuwenhoek. 1971, 37,
33-49.
13. Whiting, G.C. Lactic acid bacteria in beverages andfood, Ed. J.G. Carr,
CV. Cutting and G.C Whiting, Londoa Academic Press, 1975,69-85.
14. Whiting, G.C. Journal of the Institute of Brewing, 1976, 82, 84-92.
15. Williams, A.A. Journal of the Institute of Brewing, 1974, 80, 455-470.
Journal of The Institute of Brewing 195
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Volume 105, No. 3,1999 Journal of The Institute ofBreio'mg
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196 Journal of The Institute of Brewing
This document is provided compliments of the Institute of Brewing and Distilling www.ibd.org.uk Copyright - Journal of the Institute of Brewing