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Applied and Environmental Microbiology, April 2005, p. 1745-1753, Vol. 71, No. 4
0099-2240/05/$08.00+0 doi:10.1128/AEM.71.4.1745-1753.2005
Copyright © 2005, American Society for Microbiology. All Rights Reserved.
School of Molecular Sciences, Victoria University, Melbourne, Victoria, Australia
Received 11 May 2004/ Accepted 1 October 2004
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Another approach to gut microflora management is the use of synbiotics, for which probiotics and prebiotics are used in combination. The concept of synbiotics has been widely studied, mostly to improve the survivability of probiotics in both in vitro and in vivo experiments (5, 7) and to modulate colonic microbial populations in animal models (10, 12). However, to our knowledge, there is no information on suitable combinations of probiotics and prebiotics specifically targeting the removal of cholesterol for in vitro models, although a limited number of studies have addressed the use of prebiotics or synbiotics to reduce serum cholesterol and to regulate hepatic lipogenesis and lipid metabolism (14, 25). Yet all of these studies involved in vivo experiments, in which the true interaction patterns of synbiotics which reduce cholesterol are poorly understood.
The response surface method (RSM) is a statistical and mathematical method that involves main and interaction effects to account for curvature, to improve optimal process settings, and to troubleshoot process problems and weak points (18). It has been successfully utilized to optimize compositions of microbiological media, conditions of enzyme hydrolysis, and parameters for food preservation and fermentation processes (15). Previous studies have used conventional methods (such as one factor at one time) to evaluate the in vitro performance of probiotics and/or prebiotics in the removal of cholesterol. These methods, however, require a large number of experiments to describe the effect of individual factors and are time-consuming. Besides, no established statistical method has been introduced to distinguish the interaction effects from the main effects. Furthermore, up to now, there has been no reported study on the use of RSM to remove or reduce cholesterol by the use of either in vitro experiments or animal models. Thus, the aims of this study were to optimize cholesterol removal by Lactobacillus casei ASCC 292 in the presence of fructooligosaccharide (FOS) and maltodextrin through the response surface approach. This information will provide a better understanding of the interactions involved in cholesterol reduction for in vivo experiments.
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Six types of commercially available prebiotics were used, including sorbitol (Sigma Chemical Co., St. Louis, Mo.), mannitol (Sigma), maltodextrin (Grain Processing Corp., Muscatine, Iowa), high-amylose maize (Starch Australasia Ltd., Lane Cove, New South Wales, Australia), inulin (Orafti Pty. Ltd., Tienen, Belgium), and FOS (Orafti). High-amylose maize contained >70% amylose and 32.5% total dietary fiber. The inulin used was Raftiline ST, with a purity of 92% and an average degree of polymerization of 10. The FOS used was Raftilose P95, with a purity of 95% and an average degree of polymerization of 4.
All prebiotics and freeze-dried cells of L. casei ASCC 292 were used at concentrations as indicated in the experimental design explained below (Table 1). Prebiotic media were inoculated with freeze-dried cells of L. casei ASCC 292 at appropriate levels, as described in the experimental design.
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TABLE 1. Treatment combinations and responses for screening experiments
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Growth of L. casei ASCC 292 in the presence of prebiotics.
The growth of L. casei was determined by the plate count method. Bacilli generally divide in one plane and can produce chains of cells due to the failure to separate completely. Thus, at the end of the fermentation time, fermentation broth containing probiotic cultures was sonicated for 5 s to disrupt clumps of lactobacilli (3) before serial dilutions were performed. MRS agar was used for plating, and the plates were incubated anaerobically at 37°C for 24 h. Growth was calculated in log10 CFU (CFU per milliliter) and expressed as the percent difference between initial growth values obtained at time zero and values obtained at the end of the incubation period.
Mean doubling time.
The mean doubling time was calculated as described previously (24). The specific growth rate (µ) of the cultures was obtained by use of the following equation: µ = (ln X2 ln X1)/(t2 t1), where X2 and X1 are the cell densities at times t2 and t1, respectively. The mean doubling time (Td) was calculated as follows: Td = ln 2/µ, expressed in minutes.
Utilization of substrate and growth yield.
The utilization of substrate was determined as the difference between the initial concentrations of prebiotics and their final concentrations after the incubation period. Broths containing L. casei ASCC 292 were centrifuged at 2,714 x g at 4°C for 15 min, and the supernatants were used to determine the concentrations of residual prebiotics. Since both substrates are oligosaccharides, their residual concentrations were determined by colorimetry after hexose hydrolysis with phenol-sulfuric acid (9). Utilization of the substrate was expressed as a percentage (initial concentration over final concentration). The growth yield was expressed as growth per gram of substrate utilized. Growth was obtained by the pour plate method described above and expressed as the difference between the initial log10 CFU values per milliliter at time zero and the values at the end of the incubation period.
SCFA determination.
The fermentation of prebiotics was determined by measuring short-chain fatty acids (SCFA) as the end products of fermentation by high-performance liquid chromatography (Varian Australia Pty. Ltd., Mulgrave, Australia). At the end of the incubation period, fermentation broths containing L. casei ASCC 292 and prebiotics were centrifuged at 2,714 x g at 4°C for 15 min, and the supernatants were prepared for high-performance liquid chromatography by a previously described method (8). SCFA were expressed as the total acetic, butyric, and propionic acids.
Experimental design and statistical analyses.
Screening experiments to select prebiotics were performed with seven independent factors, namely, L. casei ASCC 292 (X1), sorbitol (X2), mannitol (X3), maltodextrin (X4), high-amylose maize (X5), inulin (X6), and FOS (X7), by use of a two-level partial factorial design (27-22) resulting in 64 experimental runs (including duplicates) and 5 middle-point runs (Table 1). A first-order empirical equation was used to exclude insignificant factors and to generate the steepest ascent, which led to optimization by a rotatable central composite design (CCD). The treatment combinations were allocated into two blocks, and all experiments were performed in 2 days. The first block, representing the first day of the experiment, contained the factorial runs accompanied by four center runs. The second block, representing the second day of the experiment, contained the axial runs accompanied by two center runs. These modeling and statistical analyses were performed by the use of Design Expert, version 5.07, software (Stat-Ease Corp., Minneapolis, Minn.).
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TABLE 2. ANOVA and coefficient estimates for evaluation of the first-order model
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TABLE 3. Steepest ascent coordination path for all chosen factors at coded and natural levels
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value of ±1.682 to produce design rotatability (2). The design matrix for CCD and the experimental responses are shown in Table 4, while adequacy and fitness were evaluated by ANOVA and calculations of regression coefficients (Table 5). The ANOVA results indicated that the quadratic regression to produce the second-order model was significant. The lack-of-fit test was insignificant, and only 4.60% of the total variation was not explained by the model. This suggested that the model accurately represents the data in the experimental region. This also indicated that second-order terms were sufficient and higher-order terms were not necessary. Probiotic, maltodextrin, and FOS levels were significant for the removal of cholesterol. It must be noted that the t value of the quadratic term of FOS (X22) was higher than others (Table 5), indicating that the second-order regression of FOS was the strongest effect. The intercept c is the estimated response at the center point, with the coded values of X1, X2, and X3 set to 0. |
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TABLE 4. CCD combination matrix using coded levels and responses
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TABLE 5. ANOVA of the second-order model and coefficient estimates for the response factor Y0 and factors X1, X2, and X3a
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(Xj) and the horizontal axis representing Xj. In this study, all Xj values have common coded levels, and thus the horizontal axis represents the common coded levels. By overlying all of the perturbation curves, we obtained a perturbation plot (20). Figure 1 shows the perturbation plot of the factors used in this study. Although all factors showed significant quadratic effects, the curve with the most prominent change was the perturbation curve of FOS compared to those of the other factors fixed at their maximum levels. Thus, we believe that FOS was the most significant factor that contributed to the removal of cholesterol and had the most pronounced quadratic effect. The probiotic showed the least prominent change compared to the other two factors, but it still showed a significant quadratic effect. |
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TABLE 6. Regression coefficients of the second-order equation for the five responsesa
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FIG. 1. Perturbation plot of probiotic (A), FOS (B), and maltodextrin (C).
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FIG. 2. Response surface for cholesterol removal from the effects of probiotic and FOS at 6.64% (wt/vol) maltodextrin (A), probiotic and maltodextrin at 4.95% (wt/vol) FOS (B), and FOS and maltodextrin at 1.71% (wt/vol) probiotic (C).
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All of these predictions by the regression model were further ascertained by a validation experiment. We compared the cholesterol removal patterns over a 24-h period by using four different media: the optimum medium (1.71% [wt/vol] probiotic, 4.95% [wt/vol] FOS, and 6.64% [wt/vol] maltodextrin), the center-point medium (1.70% [wt/vol] probiotic, 4.80% [wt/vol] FOS, and 6.80% [wt/vol] maltodextrin), the high-point medium (2.40% [wt/vol] probiotic, 7.20% [wt/vol] FOS, and 8.80% [wt/vol] maltodextrin), and the low-point medium (1.00% [wt/vol] probiotic, 2.40% [wt/vol] FOS, and 4.80% [wt/vol] maltodextrin). The cholesterol removal curves are shown in Fig. 3. Although the exact cholesterol removal quantities were different from the predictions, the patterns were in tandem with the predictions by the model. The highest levels of cholesterol were removed from the optimum medium and the center-point medium. The smallest amounts of cholesterol were removed from both the high-point and low-point media, as supported by the response surface of cholesterol removal (Fig. 2). All of these data indicated that the model produced was reliable to optimize in vitro cholesterol removal that may be used to benefit human physiological health.
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FIG. 3. Cholesterol removal by L. casei ASCC 292 in optimum ( ), center-point ( ), high-point (), and low-point ( ) media used for validation experiments. The factors used in combination for the optimum medium were probiotic (1.71% [wt/vol]), FOS (4.95% [wt/vol]), and maltodextrin (6.64% [wt/vol]). The combination used for the center-point medium was probiotic (1.70% [wt/vol]), FOS (4.80% [wt/vol]), and maltodextrin (6.80% [wt/vol]). The combination used for the high-point medium was probiotic (2.40% [wt/vol]), FOS (7.20% [wt/vol]), and maltodextrin (8.80% [wt/vol]). The combination used for the low-point medium was probiotic (1.00% [wt/vol]), FOS (2.40% [wt/vol]), and maltodextrin (4.80% [wt/vol]). Error bars represent standard errors of the means. N = 2 replicates, N = 3 sets of data/replicate, and n = 6 total observations.
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The response surface of growth (Y1) was generated based on the coded factor equation by use of the coefficients shown in Table 6. The growth increased with increasing probiotic levels from 1.00 to 1.69% (wt/vol). Further increases in the concentrations of probiotic beyond 1.69% (wt/vol) generated decreases in growth. Similarly, increments in FOS and maltodextrin concentrations from 2.40 to 4.86% (wt/vol) and 4.80 to 6.82% (wt/vol), respectively, increased the growth, but further increases in the prebiotic concentrations generated decreases in growth. All factors studied showed significant quadratic effects, as shown by the P values of the coefficient estimates. Other than the main quadratic effects, the interaction between the probiotic and maltodextrin produced the strongest influence on growth, while the interaction between the probiotic and FOS was insignificant. The response surface of growth showed similar patterns with the response surface of the removal of cholesterol, indicating a strong correlation between the removal of cholesterol and growth. We have previously shown that in vitro cholesterol assimilation is growth associated (16). Knowing this, it would be beneficial to maintain or improve the viability of Lactobacillus acidophilus ASCC 292 in in vivo models in order to favor cholesterol removal as well.
The response surfaces of substrate utilization (Y2) and growth yield (Y3) are shown in Fig. 4 and 5 and were generated based on the second-order coefficients (Table 6). Only maltodextrin produced a significant quadratic effect; the substrate utilization increased with increasing maltodextrin concentrations from 4.80 to 6.56% (wt/vol), but a further increase produced a decrease in substrate utilization. A maltodextrin-like oligosaccharide was reported to have a lower rate of fermentation than FOS and was more fermentable in the distal part of the large intestine (10). The probiotic and FOS did not produce a significant quadratic effect, but they showed significant linear correlations (Fig. 4). The interaction effects showed that only the interaction between probiotic and FOS was significant. At a higher FOS concentration (7.20% [wt/vol]), substrate utilization increased with increasing concentrations of probiotic (1.00 to 2.40% [wt/vol]). In contrast, at a low FOS concentration (2.40% [wt/vol]), substrate utilization decreased with increasing concentrations of the probiotic. This may be due to competition for the substrate with increasing cell numbers at low substrate levels. It must be noted that substrate utilization increased with increasing probiotic and FOS concentrations, despite a decrease in growth and cholesterol removal for these experimental regions. Thus, cholesterol removal may be growth associated, but both cholesterol removal and growth were not influenced solely by the utilization of FOS. This was supported by the lower growth yield at these regions (Fig. 5). Although maltodextrin did not show an overall significant interaction effect with the probiotic or FOS, it generated a significant main quadratic effect. Our results indicated that interactions between the probiotic and maltodextrin might have a stronger influence on growth and cholesterol removal at regions that were not contributed by an interaction of the probiotic and FOS. It appears that maltodextrin served as an alternative substrate when FOS was insufficient to increase the growth and subsequent removal of cholesterol. This is important for synbiotic preparation as an in vivo adjunct; FOS may be used solely or used at low concentrations coupled with maltodextrin.
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FIG. 4. Response surface for substrate utilization (%) from the effects of probiotic and FOS at 6.64% (wt/vol) maltodextrin.
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FIG. 5. Response surface for growth yield from the effects of probiotic and FOS at 6.64% (wt/vol) maltodextrin.
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The major products of the metabolism of prebiotics are SCFA, carbon dioxide, hydrogen, and bacterial cell mass (7). Although much work has been done on SCFA production and the significance of the individual fatty acids, no particular pattern of SCFA production from prebiotic fermentation has yet emerged. The amount of SCFA (Y5) was obtained as a total of individual fatty acids, namely, acetic, butyric, and propionic acids. Only the probiotic produced significant quadratic effects on SCFA production, as did interactions between (X1, X2) and (X1, X3). The response surface (Fig. 6) generated from the second-order coefficients (Table 6) showed a close correlation with substrate utilization (Fig. 4). This indicated that the production of SCFA from the fermentation of FOS was closely associated with the uptake of the substrate. However, it must be noted that increasing the concentration of probiotic at a higher level of FOS (7.20% [wt/vol]) generated a decrease in SCFA production but increased substrate utilization. The hydrolysis of FOS was repressed by the products of the hydrolysis (13). Thus, we postulate that an increase in substrate utilization in the experimental regions would generate higher concentrations of hydrolysis products and subsequently repress further SCFA production.
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FIG. 6. Response surface for SCFA production from the effects of probiotic and FOS at 6.64% (wt/vol) maltodextrin.
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