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Applied and Environmental Microbiology, March 2002, p. 1431-1435, Vol. 68, No. 3
0099-2240/02/$04.00+0 DOI: 10.1128/AEM.68.3.1431-1435.2002
Copyright © 2002, American Society for Microbiology. All Rights Reserved.
Research Group of Industrial Microbiology, Fermentation Technology and Downstream Processing (IMDO), Department of Applied Biological Sciences, Vrije Universiteit Brussel, B-1050 Brussels, Belgium
Received 30 August 2001/ Accepted 11 December 2001
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The objective of this study was to assess the suitability in sourdough fermentations of the bacteriocin-producing organism L. amylovorus DCE 471, a strong and fast acidifier with a competitive advantage (1, 2, 3). Our analysis was performed by using a basic sourdough simulation medium (SSM) and a predictive model which describes the influence on microbial behavior of the temperature and pH during sourdough fermentations.
L. amylovorus DCE 471, which was isolated from corn steep liquor and produces the bacteriocin amylovorin L471 (2), was used throughout this study. Lactobacillus delbrueckii subsp. bulgaricus LMG 6901T was used as an indicator organism to determine levels of amylovorin L471 activity (3). The strains were maintained and propagated and agar media were prepared as described previously (2).
A series of fermentations were performed in basic SSM containing (per liter) 10 g of tryptone (Oxoid, Basingstoke, United Kingdom), 12 g of yeast extract (Merck, Darmstadt, Germany), 5 g of Lab-Lemco (Oxoid), 0.5 g of cysteine-HCl, 0.2 g of MgSO4 · 7H2O, 0.05 g of MnSO4 · H2O, 2 g of KH2PO4, and 1 ml of Tween 80, as well as 10 g of maltose plus 10 g of fructose as energy sources. Lab-Lemco was added to avoid biphasic fermentation kinetics (unpublished results). Fermentations were carried out as described elsewhere (8). For preparation of the inoculum, 10 ml of SSM was inoculated with 0.5 ml of a freshly prepared L. amylovorus DCE 471 culture and incubated for 12 h at 37°C. This preculture was added to 90 ml of SSM. After 12 h of growth at 37°C, the second preculture was used to inoculate the fermentor. During the first experiments, the pH was maintained at 5.4 while fermentations were carried out at 28, 31, 34, 37, 40, and 44°C. In a second series of experiments, fermentations were carried out at a constant temperature of 37°C and at constant pH values of 4.2, 4.6, 5.0, 5.4, 5.8, and 6.4. To check the reproducibility, one fermentation (37°C, pH 5.4) was performed in triplicate, and the standard deviation was calculated. For validation of the model, two additional fermentations were performed, one at 35°C and a constant pH of 5.5 and the other at 42°C and a constant pH of 4.5.
Samples were withdrawn aseptically from the fermentor to determine biomass (as cell dry mass [CDM]), soluble bacteriocin activity (as AU), lactic acid concentration, and residual maltose, fructose, and glucose concentrations as described elsewhere (8). The standard deviations for the CDM, maltose, fructose, and lactic acid measurements were 0.11, 0.04, 0.035, and 0.02 g · liter-1, respectively.
Incubation experiments at the 100-ml scale were carried out at various temperatures and pH values to gain additional information about the growth of L. amylovorus DCE 471 cells at intermediate temperatures and pH values and to determine the growth limits of this organism.
Primary model development was performed as described by Leroy and De Vuyst (8), except that cell growth was modeled with a modification of the equation for logistic growth, maltose consumption and fructose consumption were modeled separately by using the maintenance energy model, and lactic acid production was calculated based on the consumption of both maltose and fructose (Table 1). Secondary modeling of the biokinetic parameters was performed as described by Leroy and De Vuyst (9); the
-functions for temperature (
T and pH (
pH) that were used to calculate the maximum specific growth rate (µmax) were based on the equations of Rosso (11, 12). It was assumed that there was no interaction between temperature and pH, so that µmax = (µmax)opt x
T x
pH. Where appropriate, the quadratic correlation coefficient (r2) is given below.
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TABLE 1. Equations used for primary model development
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At the temperatures used for manufacturing type I sourdoughs (<30°C), growth was slow (µmax at constant pH 5.4 < 0.25 h-1), and the bacteriocin activity was low. At the temperatures used for manufacturing type II sourdoughs (between 30 and 37°C), growth was suboptimal (0.25 h-1 < µmax at constant pH 5.4 < 0.64 h-1). Both specific amylovorin L471 production (kB) and volumetric amylovorin L471 activity in the supernatant (Bmax) were high at these temperatures. The maximum Bmax values were observed at 37°C (5,500 kAU liter-1), 40°C (5,300 kAU liter-1), and 44°C (5,100 kAU liter-1) (results not shown). Lejeune et al. (7) obtained kB values of 3,500 and 4,000 kAU g of CDM-1 when they grew L. amylovorus DCE 471 in MRS medium at a constant pH of 5.0 and at fermentation temperatures of 37 and 45°C, respectively. These values are lower than those obtained in SSM at a constant pH of 5.4, but the effect of temperature was also limited in this temperature range. Since the maximum attainable biomass concentration (Xmax) varied only slightly in this temperature range (Fig. 1a), kB followed the same trend as Bmax, and the average kB value was 5,100 kAU g of CDM-1 (Fig. 1b). At 34°C, Xmax was lower (Fig. 1a). Also, Bmax (4,300 kAU liter-1) was lower at 34°C, resulting in a kB value comparable to that found at 37 to 44°C (Fig. 1b). At lower temperatures, Bmax was significantly lower (2,800 kAU liter-1 at 31°C and 1,900 kAU liter-1 at 28°C). Also, Xmax was markedly lower (Fig. 1a). Thus, it appears that L. amylovorus DCE 471 makes better use of the complex energy and nitrogen source at 37 to 44°C than at 34°C. Since kB was very high at the lower temperatures (Fig. 1b), especially 28°C, the low level of bacteriocin activity in the supernatant was due to the small amount of biomass formed (Fig. 1a) and the high apparent rate of bacteriocin inactivation (kinact) (Fig. 1b). The maximum cell yield was obtained at pH 4.2 to 5.0 (Fig. 1c). Thus, L. amylovorus DCE 471 growth is close to the optimum value (pH 5.4) at the starting pH for sourdough fermentations (around pH 5.8). At the end of sourdough fermentations (pH near 3.8), L. amylovorus DCE 471 still grows, but it grows slowly. Specific bacteriocin production increased with increasing pH, especially at pH values greater than 5.0 (Fig. 1d). Both kB and Bmax were highest at the pH that corresponded to the pH at the onset of sourdough fermentation (between pH 5.0 and 5.8). In accordance with the findings of De Vuyst et al. for growth and bacteriocin production by L. amylovorus DCE 471 in MRS medium at 37°C when constant pH values in the range from pH 4.5 to 7.0 were used, Bmax was high at pH 5.0, 5.4, and 5.8 (2). In the pH range from pH 4.2 to 6.4, kinact increased with increasing pH (Fig. 1d), which can be explained by increased adsorption of the bacteriocin molecules to the cells at higher pH values (15).
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FIG. 1. (a, b, e, and f) Influence of temperature at a constant pH of 5.4 on L. amylovorus DCE 471 in SSM. (a) Biomass production. Symbols: , Xmax (in grams of CDM per liter); , n. (b) Bacteriocin production. Symbols: , kB (in kilo-arbitrary units [kAU] per gram of CDM); , kinact (in liters per gram of CDM per hour). (e) Fructose metabolism. Symbols: , YX/F (in grams of CDM per gram of fructose); , mF (in grams of fructose per gram of CDM per hour). (f) Maltose metabolism. Symbols: , YX/M (in grams of CDM per gram of maltose); , mM (in grams of maltose per gram of CDM per hour). (c, d, g, and h) Influence of pH at a constant temperature of 37°C on L. amylovorus DCE 471 in SSM. (c) Biomass production. Symbols: , Xmax (in grams of CDM per liter); , n. (d) Bacteriocin production. Symbols: , kB (in kAU per gram of CDM); , kinact (in liters per gram of CDM per hour). (g) Fructose metabolism. Symbols: , YX/F (in grams of CDM per gram of fructose); , mF (in grams of fructose per gram of CDM per hour). (h) Maltose metabolism. Symbols: , YX/M (in grams of CDM per gram of maltose); , mM (in grams of maltose per gram of CDM per hour). Symbols indicate experimental values; the lines were drawn by using the model.
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Figure 2a shows the relationship between temperature and µmax as calculated by using the secondary modeling approach. The optimum, minimum, and maximum temperatures for cell growth were 44, 20, and 49.8°C, respectively, illustrating the thermophilic character of L. amylovorus DCE 471. The activation energy was calculated to be 84.7 kJ mol-1 (Arrhenius plot not shown). At 37°C, the optimum, minimum, and maximum pH values for growth of L. amylovorus DCE 471 were 5.4, 3.55, and 9.0, respectively (Fig. 2b).
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FIG. 2. (a) Influence of temperature at a constant pH of 4.2 ( ), 4.6 ( ), 5.0 ( ), 5.4 ( and ), 5.8 (x, dotted line), or 6.4 (+, dotted line) on the µmax of L. amylovorus DCE 471 in SSM. (b) Influence of pH at a constant temperature of 28°C ( ), 31°C ( ), 34°C ( ), 37°C ( and ), 40°C ( , dotted line), or 44°C ( , dotted line) on the µmax of L. amylovorus DCE 471 in SSM. Symbols indicate experimental values; the open symbols for both pH 5.4 and 37°C indicate the results of small-scale incubation experiments. The solid lines were drawn by using the model.
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FIG. 3. Surface model showing the influence of pH and temperature on µmax (per hour) (a), Xmax (in grams of CDM per liter) (b), kB (in kAU per gram of CDM) (c), kinact (in liters per gram of CDM per hour) (d), YX/M (in grams of CDM per gram of maltose) (e), and mF (in grams of fructose per gram of CDM per hour) (f).
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Vincent Schrijvers is acknowledged for his technical assistance.
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