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Applied and Environmental Microbiology, March 2007, p. 1601-1611, Vol. 73, No. 5
0099-2240/07/$08.00+0 doi:10.1128/AEM.02198-06
Copyright © 2007, American Society for Microbiology. All Rights Reserved.

J. Debevere,3
F. Devlieghere,3 and
J. F. Van Impe1*
Division of Chemical and Biochemical Process Technology and Control, Department of Chemical Engineering, Katholieke Universiteit Leuven, W. de Croylaan 46, B-3001 Leuven, Belgium,1 Division of Mechatronics, Biostatistics and Sensors (MeBioS), Department of Biosystems (BIOSYST), Katholieke Universiteit Leuven, W. de Croylaan 42, B-3001 Leuven, Belgium,2 Laboratory of Food Microbiology and Food Preservation, Department of Food Safety and Food Quality, Ghent University, Coupure Links 653, B-9000 Ghent, Belgium3
Received 19 September 2006/ Accepted 22 December 2006
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The organic acid antimicrobial activity is twofold: (i) release of protons at dissociation lowers the extracellular pH, and (ii) the undissociated form of the acid is able to diffuse into the cell, affecting the cell metabolism. The latter effect is reported to result in a global inhibition due to acidification of the cytoplasm and a more specific inhibition of several metabolic and anabolic functions (1, 23, 35). The said antimicrobial activity can reveal itself in (i) inhibition, i.e., an early induction of the stationary phase, and (afterwards) (ii) inactivation, i.e., a decrease in cell concentration to values below the detection limit of the so-called target (pathogenic or spoilage) organism.
In predictive microbiology, the knowledge of microbial growth or death responses to environmental factors is translated into mathematical equations that enable prediction of microbial proliferation or inactivation in foods. Final application lies in the quantitative assessment of the microbial safety and quality of food products, e.g., in defining the critical control points within a hazard analysis and critical control point framework, in shelf-life studies (27), or in the exposure assessment step within microbiological risk assessments. Some models had already been developed to describe the influence of organic acids such as lactic acid on the evolution of the target organism, not only in pure culture but also in coculture with a lactic acid bacterium (19, 21, 22, 31, 40, 46). However, the individual effects of the factors undissociated lactic acid [LaH] and pH are still insufficiently quantified, especially for inactivation processes. To the best of the authors' knowledge, in only one study (9) was a model developed that describes the inactivation of Listeria monocytogenes as a function of pH and undissociated lactic or acetic acid. The differentiated effects of pH and undissociated acid were expressed as influencing t4D, the time to a four-decimal-reduction inactivation (99.99%), and, unfortunately, no predictions of cell concentration at any time instance before or after t4D could be made.
This study investigated the inactivation of L. innocua at controlled conditions of pH and [LaH]. The experimental setup was constructed to enable us to separate the effects of pH and [LaH], in contrast to several previous studies (19, 46) where pH and [LaH] had a one-to-one relationship defined by the buffer capacity of the medium.
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Because of the observed variability for some of the experimental conditions (explained later in this text), replicate experiments were performed in parallel (i.e., at the same time). To avoid the possible influence of differences in preculturing conditions of inocula for these experiments, precultures were prepared as described above. However, before the first centrifugation step, precultures for parallel experiments were mixed and again separated into two parts, assuming identical inocula were obtained. Thereafter, the preculture treatment proceeded as described above.
Experimental conditions.
Inactivation experiments were performed in 1-liter Erlenmeyer flasks (Duran Schott) provided with a side arm. Both openings (upper and side arm) were closed with screw caps containing a rubber septum. The Erlenmeyer flask was filled with 550 ml of a rich, modified brain heart infusion medium containing BHI (37 g/liter; Oxoid) supplemented with yeast extract (4 g/liter; Oxoid), glucose (18 g/liter; VEL), Tween 80 (1 ml/liter; Merck), MgSO4 · 7H2O (0.2 g/liter; Acros), and MnSO4 · H2O (0.04 g/liter; Acros). Before inoculation, the medium was flushed with N2 to create an anaerobic atmosphere. The tested combinations of pH0 and [LaH]0 are graphically presented in Fig. 1. Conditions for which parallel experiments with mixed inoculum were performed are indicated in a box. A combination of initial pH (i.e., pH0) and initial concentration of undissociated lactic acid (i.e., [LaH]0) was set as follows. For clarity, the procedure is illustrated for setting pH0 = 3.5 and [LaH]0 = 0.05 M, as indicated by the thick box in Fig. 1. First, the pH of the medium was adjusted to a certain so-called "pH*" by the addition of the appropriate volumes of HCl (1 N; Acros) or KOH (0.10 g/liter; Acros). For the example, pH* equaled 3.99 (Fig. 1). In the second step, L(+)-lactic acid (Acros) was added. By preliminary experiments, it was ensured that the effective concentration of lactic acid was not dependent on poly-lactic acid formation. Because of its high viscosity, measurements of weight of lactic acid were more accurate than volumetric measurements. Therefore, for most of the experiments, the mass of lactic acid necessary to reach the appropriate initial concentration of total lactic acid (i.e., LaHtot,0; initial sum of both the dissociated and undissociated forms) was added (LaHtot,0 = 0.0718 M in the example). As a consequence, the pH of the medium decreases from pH* on (according to the lower titration curve indicated in Fig. 1). If the resulting pH (3.37 in the example) was slightly different from the desired pH0 (e.g., 3.5) a second pH adjustment was performed, reaching the desired conditions (pH0 = 3.5 and [LaH]0 = 0.05 M in the example). No extra buffers were added. Approximately 15 h before inoculation, flasks were placed on a rotary shaker (130 rpm; Heidolph Unimax 2010) in a cooling incubator at 12°C (cooling incubator series 6000; Termaks). Listeria innocua was inoculated at a concentration of approximately 108 CFU/ml. During the experiment, temperature was maintained at 12°C to ensure a possible coupling with microbial growth models recently developed by our research group (45, 46).
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FIG. 1. Overview of the 30 pH0-[LaH]0 combinations tested. Eleven of these combinations were situated on the titration curve with pH* = 6.20 (+), and 19 formed a more or less rectangular shape ( ). Condition symbols surrounded by a box correspond to experiments performed in parallel. The experiments with pH0-[LaH]0 combinations equal to 4.0 for pH0 and 0 M for [LaH]0 were performed in duplicate (4.13 and 0.0210 M, respectively) threefold, and the experimental condition (3.75 and 0 M, respectively) was investigated fourfold.
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Measurements.
At regular time intervals, samples (6 ml) were taken with a sterile syringe (Discardit II; Becton Dickinson) and needle (Microlance 3; Becton Dickinson) through the side septum. Cell concentration was determined by plating a dilution series of 1 ml of the sample (in peptone water) by means of a spiral plater (Eddy Jet, D-mode; IUL Instruments) on a selective medium based on the modified BHI medium, supplemented with LiCl (5 g/liter; UCB) and agar (18 g/liter; Oxoid). LiCl was added to enable possible future comparison with coculture experiments, as described by Vereecken et al. (45). Plates were incubated at 37°C for 24 to 48 h for samples at the end of the inactivation process. The remaining 5 ml of the sample was filtered over a membrane filter (Filtropur S 0.2; Sarstedt) to remove the cells. The pH of the supernatant was determined with a pH sensor (inoLab level 1; WTW) (accuracy of ±0.005 as stated by the producer). The lactic acid concentration in the sample was measured by gas chromatographic determination of the methyl ester. In sequential order, 0.1 ml ß-hydroxybutyric acid (Merck Schuchardt) (internal standard), 1 ml H2SO4 (50%; Fisher Scientific), and 4 ml methanol (Acros) were added to 1.9 ml of the filtrate. Next, the mixture was heated to 55°C for 30 min. Afterwards, 2 ml distilled water and 1 ml chloroform (Acros) were added, and the mixture was shaken for 2 min. After separation of the aqueous and chloroform phases, 5 µl of the chloroform phase was injected into the gas chromatograph (Finnigan Trace GC Ultra), equipped with a flame ionization detector. Separation occurred on a 2-m column with 10% Carbowax 20 M on Chromosorb W-AW 80/100 (settings: gas flow, mobile phase [N2], 40 ml/min; detection [H2 plus air], 25 ml/min; temperature of column, 120°C; temperature of injection block, 240°C; and temperature of detection block, 245°C). By means of a calibration curve, peak factors equal to the ratio of the peak surface for lactic acid and the peak surface for ß-hydroxybutyric acid were related to the lactic acid concentration in the sample. For the lactic acid measurements, a standard error of 8.420 · 103 was obtained when the measured and calculated (based on mass of lactic acid added) LaHtot,0 values were compared. The glucose concentration was determined with an enzymatic probe (Granutest; Merck).
For the experiments performed in duplicate and situated on the titration curves with pH* different from 6.20 (Fig. 1), the behavior of the cells during the exposure to adverse conditions was monitored. At regular time instances, a sample was inspected by oil immersion phase-contrast microscopy with an Olympus BX51 (objective, Ach 100x/1.25 oil [pH 3]; Olympus, Japan) to detect the formation of cell aggregates and their amount and morphology.
In addition, for an initial pH of 3.75, the effect of an increasing initial concentration of undissociated lactic acid (0 M, 0.0400 M, and 0.0610 M) was investigated through fluorescence microscopy. Cells were stained with carboxyfluorescein diacetate (cFDA; 1 mM in acetone [Molecular Probes, Leiden, The Netherlands]) and propidium iodide (PI; 2 mM in water [Molecular Probes]). A sample representing each experimental condition at viable cell concentrations of 104 (0 M), 105 (0.0400 M), and 106 (0.0610 M) CFU/ml was investigated. For this purpose, 100 µl of cell suspension was centrifuged (10 min at 4,660 x g; Biofuge pico [Heraeus Instruments, Brussels, Belgium]) and washed with phosphate-buffered saline (PBS; 50 mM, pH 7.2, consisting of 5.675 g/liter Na2HPO4 and 1.36 g/liter KH2PO4) for two times. Next, 1 µl of cFDA and 1.5 µl of PI were added to 100 µl of cell suspension in PBS. After incubation for 10 to 15 min in the dark at room temperature, samples were placed on ice. For each sample, five fluorescence images were taken with a Carl Zeiss Axio Imager A.1 (objective; Zeiss EC Plan-Neofluar, 100x/1.3 oil, pH 3; camera, Zeiss AxioCam MRm) and analyzed with an AxioVision LE V4.4 (Carl Zeiss Vision GmbH).
Modeling.
Quantification of the individual effects of the concentration of undissociated lactic acid ([LaH]0) and the pH (pH0) was performed in two steps. First, a primary model suitable to describe the observed inactivation curves was selected. Second, variation of the primary model parameters with [LaH]0 and pH0 was translated into a polynomial or double-exponential expression.
(i) Determination of primary inactivation kinetics.
For the modeling of the experimental data, GInaFiT (version 1.4), a freeware add-in for Microsoft Excel, was used (14). This software tool can calibrate the following models to the experimental data: (i) the traditional log-linear model (e.g., see reference 3), (ii) the log-linear model with shoulder and/or tail (13), (iii) Weibull-type models (2, 24), and (iv) a biphasic model (10) and a newly proposed biphasic model with a preceding shoulder period (14). Next to the parameter values, the tool also computes statistical measures such as the sum of squared errors (SSE), the mean sum of squared errors (MSE), and the root mean sum of squared errors (RMSE). The last criterion is useful in assessing whether a given model (linear or nonlinear) truly fits the data well, namely, its magnitude should be similar to the magnitude of the experimental error (33).
(ii) Secondary model describing the separate effects of [LaH]0 and pH0.
The (individual) effects of [LaH]0 and pH0 on the microbial inactivation curves could be translated into the variation of the primary model parameters as a function of both factors. As will be shown in Results, the Weibull (or Weibull-type) model was selected as a primary model. The model equation can be written as follows, where t (h) is time, N(t) (CFU/ml) is the cell concentration as a function of time, N0 (CFU/ml) is the initial cell concentration,
(h) is the time of the first log reduction, p () is the shape factor, p > 1 is a convex shape, p < 1 is a concave shape, and p = 1 is a log-linear shape (24):
![]() | (1) |
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A secondary model for the variation of the Weibull parameters p and
as a function of [LaH]0 and pH0 was developed. To facilitate the parameter estimation procedure, the [LaH]0 and pH0 data were centered around 0 and rescaled by subtracting their mean value ([LaH]0 = 2.828 x 102, pH0 = 3.89) and dividing by their standard deviation (s[LaH]0 = 2.113 x 102 and
= 3.252 x 101) (28). A second-order polynomial model was proposed for the variation of ln(
) with the centered and scaled [LaH]0 and pH0 values. Partial F tests were used to find significant terms. Prediction of
(that is, the original, untransformed values) was obtained by taking the antilogarithm of the fitted values, and a correction term for bias was included (26).
For p, a more complex model structure similar to the modified Gompertz equation for microbial growth described by Zwietering et al. (50) or the switching function applied by Van Impe et al. (43) was proposed.
The 95% confidence intervals for the secondary model parameters were calculated based on the variance-covariance matrix as, for example, described by Van Impe and coworkers (44).
For the processing of the experimental data and the parameter estimations for the secondary model, Matlab (version 6.1 R12; The MathWorks Inc., Natick, MA) was used.
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FIG. 2. L. innocua inactivation at pH0-[LaH]0 combinations on the titration curve with pH* equal to 6.20 for the full-time range (a) and a detailed view for time zero to 200 h (b).
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Inactivation at pH0-[LaH]0 combinations forming a ± rectangular shape.
The resulting inactivation curves for 18 of the 19 pH0-[LaH]0 combinations tested are presented in Fig. 3. The inactivation curves showed also a (sometimes almost negligible) shoulder period followed by a decrease of the cell concentration to values below the detection limit. The inactivation curves with [LaH]0 within 0.0370 to 0.040 M (Fig. 3c) or pH0 equal to 4.01 or 4.48 (Fig. 3f) showed a tail-like behavior. The cell concentration decreased slowly to values below the detection limit. Again, depending on the conditions, the descent phase consisted of one or two log-linear parts with the respective slopes.
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FIG. 3. Inactivation of L. innocua at pH0-[LaH]0 combinations situated in the rectangular shape. (Top) Influence of [LaH]0 at pH0 values of ±3.5 (a), 4.0 (b), and 4.5 (c). (Bottom) Influence of pH0 at [LaH]0 values of 0 M (d), ±0.025 M (e), and ±0.037 M (f).
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Similar to the experiments described in the previous section, glucose concentration (data not shown) remained constant during the inactivation process. pH and lactic acid measurements (not shown) sometimes showed an increase during the course of the experiment. For 23.3% of the experiments, total lactic acid increased by more than 0.01 M with an increase in pH higher than 0.2 (all had a shoulder period of >380 h). Only one experiment (3.3%) had similarities to the previous category, but had a less high lactic acid increase (0.005 M). A total of 13.3% of the experiments were characterized by constant lactic acid and pH profiles (four experiments with pH0 = 3.5). For 50% of the experiments, the lactic acid concentration remained constant, but pH increased (less than 0.2). These experiments all had a shoulder period shorter than 380 h. Only 10% of the experiments showed a slight lactic acid decrease, while pH increased for a maximum of 0.2.
Variability in the observed inactivation curves.
After all the collected inactivation curves were compared, a certain variation became visible: (i) inactivation curves for identical pH0-[LaH]0 conditions (for experiments performed in duplicate) did not show identical evolution, and (ii) in the vicinity of the growth/no growth interface, the inactivation process seemed to be a rather contradictory process.
The first type of variation is illustrated in Fig. 3 and 4. Almost identical conditions of [LaH]0 and pH0 in, for example, Fig. 3a and d and 4a did not show identical behaviors of the inactivation curve. Mostly, duplicate experiments showed equal lengths of the shoulder period, but different slopes in the descent phase. Furthermore, this variation seemed to depend on the severity of the pH0-[LaH]0 conditions as a lower pH0 and/or a higher concentration of undissociated lactic acid (so more stressful conditions) in Fig. 4b exhibited almost no difference in the inactivation curves.
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FIG. 4. Variation in inactivation for (almost) identical pH0-[LaH]0 conditions.
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FIG. 5. Variation in inactivation for pH0-[LaH]0 conditions near the growth/no growth interface.
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Microscopic behavior of the L. innocua cell during the inactivation process.
Microscopic observations of the cell behavior at regular time instances during the inactivation process (for the duplicate experiments) led to the following results. In the beginning of the experiment, and approximately for the length of the shoulder phase, mainly individual cells were observed. In addition, extended cells or long filaments were visible which seemed to show small incisions about one cell length from each other (Fig. 6a). However, when the cell concentration started to decrease, cell aggregates were formed. Cell clumps became clearly visible at a viable cell concentration of 105 to 106 CFU/ml (Fig. 6b). Only for the experiment with pH0-[LaH]0 conditions equal to 4.49 for pH0 and 0.0408 M for [LaH]0 did the cell clumps disintegrate when the viable cell concentration was around the detection limit (102.5 CFU/ml). Thereafter, viable cell concentration increased again (not shown).
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FIG. 6. Microscopic observations of the cell behavior during the inactivation process. (a) Individual cells, extended cells, and long filaments. (b) Cell clumps.
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TABLE 1. Percentage of cells per category for the fluorescence images
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FIG. 7. Description of L. innocua inactivation by the four types of inactivation models included in GInaFiT. Inactivation at (a) pH0 = 3.49 and [LaH]0 = 0.0504 M, (b) pH0 = 4.37 and [LaH]0 = 0.0153 M, and (c) pH0 = 4.34 and [LaH]0 = 0.0269 M.
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and p.
The following equations were calibrated on the ln(
) and p data, respectively:
![]() | (2) |
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![]() | (3) |
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) in equation 2 and a term for [LaH]0 for pmin in equation 3 to be insignificant. The resulting parameter values for equations 2 and 3 are presented in Table 2. As can be seen, the 95% confidence intervals for the parameters were small in comparison to the parameter values themselves, which means that all parameters took reliable values. Moreover, based on the value of R2 (or R2adj), approximately 93 and 84% of the variability in the ln(
) and p data were explained by, respectively, model equations 2 and 3 together with their optimal parameter values. |
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TABLE 2. Resulting parameter values and their 95% confidence intervals for the calibration of equations 2 and 3 to the ln( ) and p data, respectivelya
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(i.e., the untransformed values) was obtained by taking the antilogarithm of ln(
) as depicted below.
![]() | (4) |
R2 was used as a correction term for bias and is equal to the sum of squared errors for the regression model to the transformed data divided by the degrees of freedom (26). In Fig. 8, the prediction of
and p as function of pH0 and [LaH]0 is graphically presented. To illustrate the application of the developed models in the food industry, the conditions of pH0 or [LaH]0 necessary to ensure a predetermined inactivation within a predetermined time range can be predicted by the developed models. When one wants to obtain a 2-log reduction (x = 2 in Fig. 9) of the microorganism within a time range of 48 h, a total lactic acid concentration of 0.05 M would be necessary in combination with a pH0 of 3.57 or a total lactic acid concentration of 0.07 M or 0.110 M in combination with a pH0 of 3.64 and 3.75, respectively. Note that here the conditions are shown with LaHtot,0, as this is the method used for practical application. The use of lactic acid in, for example, sprays for carcass decontamination, salad dressings, and feta cheeses can be based on the developed models (18, 23, 29).
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FIG. 8. Simulation of the evolution of (a) and p (b) as function of pH0 and [LaH]0 by means of equations 4 and 3, respectively. Data for and p situated above the model surface are indicated by asterisks; data below the surface are indicated by open circles.
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FIG. 9. Prediction of the log reduction (xD reduction) obtained within 48 h for different LaHtot,0 concentrations as a function of pH0.
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In contrast, Stumbo (41) presented a curve which can be expected under certain circumstances of thermal treatment and which does show a biphasic behavior with a more steep second decline phase. The curve is redrawn in Fig. 10 for clarity. Charles Stumbo explained this unusual biphasic behavior by the existence of cell clumping. In a slow descent phase, the (small) amount of individual cells is inactivated and the number of viable cells per clump is reduced. Then, when each clump contains only one viable cell, a fast descent phase follows which represents the decrease in colony counts originating from one viable cell. The last phases are indicated in Fig. 10 by the symbols b and c, respectively. Thus far, similarity to the biphasic inactivation process observed in our study is possible. However, Stumbo described the existence of a combined flocculation and death phase (a in Fig. 10) before the first slow descent phase during which cell clumps are formed. As a consequence, colony counts (originating from cell clumps now instead of individual cells) decreased. In the present inactivation process, this descent phase was not observed; neither did microscopic observations show cell clumping from the beginning of the experiment on. Cell clumping was observed at a viable cell concentration of approximately 106 CFU/ml, which was already in the descent phase.
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FIG. 10. Inactivation curve to be expected when a flocculation phase occurs during the early phase of the inactivation process (as per Stumbo [41]).
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It is imaginable that, depending on the conditions, the pH0 and [LaH]0 effects occur at distinct moments in the inactivation process, resulting in different (log-linear) parts in the descent phase (see, for example, pH0 equal to 4.0 and 4.34 in Fig. 3e). In addition, it is possible that for other pH0-[LaH]0 conditions, the effect of one factor dominates the other, resulting in an inactivation curve with a shape different from biphasic (like log-linear and concave shapes, for example, for pH0 equal to 3.5 in Fig. 3a). It has to be remarked that the real effect of pH or undissociated lactic acid on the cell metabolism has to be investigated in detail and has not been proven in this study. The changing shape of the inactivation curve is also reflected in the values of the parameter p of the Weibull-type model. Indeed, from Fig. 8b it can be concluded that when conditions become more stressful (i.e., lower pH0 and/or higher [LaH]0), p decreases from values above 1 (i.e., convex shape), over values equal to 1 (i.e., log-linear inactivation), to values lower than 1 (i.e., concave shape).
Variability on inactivation curves.
Increased variance in the bacterial response to less favorable conditions has been widely reported in literature (25, 32). This nonhomogeneous response of microbial populations to stress conditions is explained by differences in cell age, different states in the cell cycle, or variations in the concentrations of transcription factors (8). As described in Materials and Methods, variation in the cell suspension for the experiments with identical pH0-[LaH]0 conditions (and performed in parallel, see Fig. 1) was circumvented by starting from a mixed inoculum. In spite of that, this does not preclude the occurrence of a minor difference in processes in one of the first stages of the inactivation process, which becomes enlarged as the inactivation proceeds. As indicated above, errors on plate counting and sampling procedures were small and showed a difference in intracellular factors. Other studies reporting results of inactivation experiments performed in replicate often take the mean of the observations to work with (17, 48), which implies the existence of variation, sometimes indicated with error bars. This research indicates that this variation is large in the neighborhood of the growth/no growth interface and shrinks when conditions become more stressful: compare, for example, the inactivation curves for pH0 equal to ±4.0 in Fig. 3b, pH0 set at ±3.76 in Fig. 3d (both with [LaH]0 = 0 M), and pH0-[LaH]0 conditions of 3.5 and 0.05 M, respectively, in Fig. 4b.
Concerning the microscopic results for the behavior of the L. innocua cell during the inactivation process, the existence of long cell filaments with septa was already observed by other researchers (5, 15, 49). In addition, in the estimation of the Listeria population in a food product under adverse environmental conditions, the observed cell clumping and filament formation might comprise a problem. The viable cell concentration is possibly underestimated, resulting in erroneous conclusions concerning food safety. Also the ability of cell clumps to disintegrate and to start growing again after a certain period under some conditions of pH0 and [LaH]0 would mean a risk to food safety.
The results presented in this study clearly confirm the existence of distinct, individual effects of an initial pH and initial undissociated lactic acid concentration on the L. innocua inactivation. The process was investigated for 30 controlled pH0-[LaH]0 conditions, and four shapes of inactivation curves could be distinguished. Repeated experiments indicate that the inactivation process is characterized by a certain variability, which seems to be dependent on the severity of the conditions or otherwise stated the distance to the growth/no growth interface. Based on combination of the calibrated primary and secondary models, one can predict which conditions of pH0 or [LaH]0 are necessary to obtain a predetermined inactivation within a predetermined time range.
Scientific responsibility is assumed by the authors.
Published ahead of print on 5 January 2007. ![]()
Present address: Federal Agency for the Safety of the Food Chain, WTC III, Simon Bolivarlaan 30, B-1000 Brussels, Belgium. ![]()
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lehrádek-type models for prediction of bacterial growth in foods. J. Appl. Bacteriol. 71:452-459.
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