optimisation for high cell density cultivation of lactobacillus salivarius bbe 09-18 with response...
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Optimisation for high cell density cultivation of Lactobacillus salivarius BBE 09-18 withresponse surface methodology
Zixing Dong, Lei Gu, Juan Zhang, Miao Wang, Guocheng Du, Jian Chen, HuazhongLi
PII: S0958-6946(13)00202-1
DOI: 10.1016/j.idairyj.2013.07.015
Reference: INDA 3561
To appear in: International Dairy Journal
Received Date: 24 October 2012
Revised Date: 20 July 2013
Accepted Date: 29 July 2013
Please cite this article as: Dong, Z., Gu, L., Zhang, J., Wang, M., Du, G., Chen, J., Li, H., Optimisationfor high cell density cultivation of Lactobacillus salivarius BBE 09-18 with response surfacemethodology, International Dairy Journal (2013), doi: 10.1016/j.idairyj.2013.07.015.
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Optimisation for high cell density cultivation of Lactobacillus 1
salivarius BBE 09-18 with response surface methodology 2
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Zixing Dong a, c, Lei Gu a, c, Juan Zhang a, c, *, Miao Wang d, Guocheng Du a, c, Jian 6
Chenb, c, Huazhong Li a, c* 7
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a Key Laboratory of Industrial Biotechnology, Ministry of Education, Jiangnan 10
University, Wuxi 214122, China 11
b National Engineering Laboratory for Cereal Fermentation Technology, Jiangnan 12
University, Wuxi 214122, China 13
c School of Biotechnology, Jiangnan University, Wuxi 214122, China 14
d School of Food Science and Technology, Jiangnan University, Wuxi 214122, China 15
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* Corresponding authors. Tel: +86-510-85918307 17
E-mail addresses: [email protected] (J. Zhang); [email protected] (H. 18
Li). 19
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___________________________________________________________________23
Abstract 24
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Based on the nutritional and physiological requirements of lactic acid 26
bacteria (LAB), the effects of different carbon sources, nitrogen sources, buffer salts, 27
microelements and growth factors on the growth of Lactobacillus salivarius BBE 28
09-18 (L. salivarius BBE 09-18) were investigated, among which three key factors 29
were determined and optimised by response surface methodology. Estimated optimal 30
conditions of the factors for the growth of L. salivarius BBE 09-18 determined. 31
After cultivated in this optimised medium for 18 h at 37 °C, the viable cell count for 32
L. salivarius BBE 09-18 was 5.94×109 cfu mL-1, which was about 3 times higher 33
than that obtained in standard Man Rogosa Sharpe medium. This study will lay a 34
solid foundation for the high cell density cultivation of L. salivarius BBE 09-18 to 35
circumvent bottlenecks encountered in the production of LAB starters and probiotic 36
ingredients in the field of dairy. 37
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1. Introduction 39
40
Lactobacillus salivarius is a homofermentative microorganism that is 41
commensal in the human vagina, intestines, and oral cavities. Due to its ability to 42
grow in non-ideal conditions, such as high salt conditions, L. salivarius is somewhat 43
unique among probiotics (Charteris, Kelly, Morelli, & Collins, 1998). The strain 44
used in this study, L. salivarius BBE 09-18, has been reported to produce bacteriocin 45
(Miao, Zhen, & Xiao, 2006), which might be employed by the food industry to 46
replace chemical preservatives in foods with limited shelf life, or those foodstuffs 47
exhibiting a high risk of being contaminated by pathogen (Corr et al., 2007). This 48
strain can also lower the cholesterol level in vitro (Miao et al., 2006), and this makes 49
oral administration of viable cells to control the serum cholesterol levels of 50
hypercholesterolaemic individuals seem promising. Furthermore, it has been 51
demonstrated that this bacterium can remove cyanobacterial toxin microcystin-LR 52
(MC-LR), which can be used to deal with the MC-LR contaminated foods (Wang, 53
Zhang, Wang, Du, & Chen, 2010). All of these features make L. salivarius BBE 54
09-18 a good candidate for use as starters and probiotic ingredients for the 55
production of yoghurt, cream, cheese, and other dairy products. 56
With the growing popularity of probiotic functional foods and beverages 57
among consumers, high cell density cultivation of lactic acid bacteria (LAB) such as 58
Lactobacillus is becoming increasingly important. The growth of lactobacilli is 59
greatly influenced by fermentation conditions such as medium composition, pH, 60
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temperature, dissolved oxygen tension (DOT) and the effects of metabolites 61
(Gilliland, 1985). As LAB are fastidious about nutritional requirements, a rich 62
medium is needed for good growth (Aasen, Møretrø, Katla, Axelsson, & Storrø, 63
2000). Factors to be considered in the formulation of rich medium are costs, ability 64
to produce a large number of cells and simple harvesting methods. 65
Response surface methodology (RSM) consisting of factorial design and 66
regression analysis is more appropriate to be applied to multifactor experiments. 67
RSM is a collection of statistical techniques for designing experiments, establishing 68
models, estimating the effects of factors, and finding optimal conditions of factors 69
for desirable responses (Montgomery, 2008). The relationships between a response 70
and some related factors are quantitative, which includes the interactions and covers 71
the experimental range tested. The models built can be employed to calculate any or 72
all combinations of variables, and their effects within the test range. This method has 73
been widely used for the optimisation of culture conditions (Teng & Xu, 2008) and 74
medium composition (Liew, Ariff, Raha, & Ho, 2005; Lim, Rahim, Ho, & 75
Arbakariya, 2007; Liu et al., 2010) for various fermentation processes. However, 76
because of the specific metabolic characters and nutritional requirements, RSM has 77
rarely been applied to the cultivation of L. salivarius. 78
The main purpose of this study was to find the optimal conditions of 79
significant factors that affected the cell concentration of L. salivarius BBE 09-18. 80
The effects of different carbon sources, nitrogen sources, buffer salts, microelements 81
and growth factors on the growth of L. salivarius BBE 09-18 were studied by 82
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“change one factor at a time” method. Consequently, three main factors that had 83
significant enhancement effect on the growth of this bacterium were determined by 84
factional factorial design and optimised with RSM. Finally, the optimal conditions 85
obtained were tested for the high density cultivation of L. salivarius BBE 09-18 that 86
can be used as starters and probiotic ingredients in the dairy industry. 87
88
2. Materials and methods 89
90
2.1. Bacterial strains, medium composition, and growth conditions 91
92
The bacterium, L. salivarius BBE 09-18, isolated from the faeces of infants and 93
proven to have ideal probiotic properties (Miao et al., 2006), was used throughout 94
the study. It was kindly provided by School of Food Science and Technology, 95
Jiangnan University. 96
The composition of standard de Man, Rogosa, Sharpe (MRS) medium, pH 97
6.1-6.2, is as follows (L-1): glucose, 20 g; peptone, 10 g; beef extract, 10 g; yeast 98
extract, 5 g; sodium acetate anhydrous, 5 g; K2HPO4, 2 g; ammonium citrate dibasic, 99
2 g; MgSO4·7H2O, 0.58 g; MnSO4·4H2O, 0.25 g; Tween-80, 1 mL. Uracil and 100
guanine were dissolved in boiling distilled water and acidified with enough HCl to 101
effect solution; folic acid and nicotinic acid were dissolved in 20% (v/v) ethanol in 102
water. All these solutions were filter-sterilised and kept at 4 °C in the dark. 103
The cells of L. salivarius BBE 09-18 were stored at -80 °C in 30% (v/v) glycerol. 104
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For inoculum preparation, the stock culture was sub-cultured in a 250 mL Erlenmeyer 105
flask containing 50 mL MRS broth at 37 °C for 16 h to give a final cell concentration 106
of approximately 107 colony forming units (cfu) mL-1. The cultivation experiments 107
were conducted in 250 mL Erlenmeyer flasks containing 100 mL culture medium and 108
2% (v/v) inoculum. The flasks were incubated at 37 °C for 18 h under stationary 109
conditions and no pH control was employed during the cultivation experiments. 110
Finally, the cells were harvested at the end of the cultivation for analysis. 111
112
2.2. Analytical determination 113
114
To determine the number of viable cells (cfu), serial 10-fold dilutions of each 115
sample in sterile saline solution were plated in triplicate onto MRS agar plates. The 116
plates were then incubated at 37 °C for 48 h before enumeration. Each colony was 117
derived from a single viable cell or a colony forming unit. The final pH of the medium 118
was measured by pH/mV meter (UB-7, Denver, USA). All the results are the average 119
of three replicates. 120
121
2.3. Optimisation of carbon sources, nitrogen sources, buffer salts, microelements 122
and growth factors 123
124
The “change one factor at a time” method widely used as a traditional 125
technique for multifactor experimental design (Lim et al., 2007) was employed in 126
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this study. Different carbon sources or nitrogen sources at the concentration of 2% 127
(w/v) were used to replace those already present in standard MRS medium, 128
respectively, while all other components were maintained at a fixed level. The 129
number of viable cells and the production cost were then analysed together to choose 130
the best medium component. The effectiveness of the components is the first 131
consideration. 132
After determining the optimal carbon source and nitrogen source, we studied 133
the effects of different buffer salts, microelements, and growth factors on the cell 134
concentration of L. salivarius BBE 09-18. Medium without supplementation was 135
used as a control. Promising medium components were then chosen for subsequent 136
research. 137
138
2.4. Response surface methods and statistical analysis 139
140
In the first step, a five-factor-2-level (2III5-2) factional factorial design (FFD) 141
was performed in triplicate to identify the most significant factors strongly affecting 142
the growth of L. salivarius BBE 09-18, while unimportant factors were discarded in 143
the following experiments. The linear model obtained can be expressed according to 144
the following equation: 145
0
1
n
i i
i
Y b b X=
= +∑ (1) 146
where b0 is the intercept term; bi is the regression coefficients; Xi is the 147
corresponding natural value and n is the number of the factors. The viable count of L. 148
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salivarius BBE 09-18 was defined as dependent variable or response (Y). 149
To arrive in the domain of the optimum of the significant factors, the 150
steepest ascent method was used. This design whose direction was parallel to the 151
response of Eq. (1) began from the centre point of the factorial design and increased 152
as direction ratio of regression coefficient βi. The experiments were conducted until 153
no further increase of the response and the point in the expected experimental scope 154
was used as the centre point for further optimisation studies. 155
Finally, a central composite design (CCD) containing 6 centre runs, 8 156
factorial runs, and 6 axial runs was applied to allocate treatment combinations in this 157
experiment. With the viable count of L. salivarius BBE 09-18 as response, a 158
quadratic model was generated, which was made up of trials plus a star configuration 159
to determine quadratic effects, and central points to estimate the pure process 160
variability and reassess gross curvature. The quadratic model obtained can be 161
expressed as follows: 162
2
0 i i ii i ij i jY X X X Xβ β β β= + + +∑ ∑ ∑ (2) 163
where β0, βi, βii, and βij are the regression coefficients variables for intercept, linear, 164
quadratic, and interaction terms, respectively. Xi and Xj are the coded values of the 165
factors chosen. Y represents the response variable. 166
All designs and calculations were carried out by Design Expert Software 167
(Version 8.0.5.0, State-Ease, Minneapolis, MN, USA). The results were analysed to 168
estimate the effects of factors and the analysis of variance (ANOVA) technique was 169
employed to identify the statistically significant factors. 170
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171
3. Results and discussion 172
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3.1. Optimisation of carbon sources and nitrogen sources 174
175
Different carbon sources and nitrogen sources at a concentration of 2% (w/v) 176
were used in this study, which was determined according to the results of 177
preliminary experiments (data not shown). As shown in Fig.1, the 178
growth-stimulating effects of monosaccharides and disaccharides were better than 179
those of polysaccharides. Among the carbon sources tested, maltose was the best for 180
the cultivation of L. salivarius BBE 09-18 with viable count of 1.88×109 cfu mL-1, 181
and α-lactose was second only to it, with 1.83×109 cfu mL-1. Nevertheless, starch 182
and other polysaccharides were not easily metabolised by this strain. Considering the 183
higher cost of maltose, α-lactose was chosen as the best carbon source. 184
Fig. 2 illustrates the effects of various nitrogen sources (2%, w/v) on the 185
biomass of L. salivarius BBE 09-18. In this study, peptone, soya, peptone, tryptone, 186
yeast extract, beef extract, ammonium sulphate, sodium nitrate, and urea were 187
separately chosen as main nitrogen source. The results showed that organic nitrogen 188
sources could significantly enhance the cell concentration, while inorganic nitrogen 189
sources were ineffective in stimulating the cell growth. Yeast extract was the best 190
among various nitrogen sources (the number of viable cells was 2.31×109 cfu mL-1), 191
which is due to its abundant nitrogen compounds, vitamins, purine and pyrimidine 192
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bases (Liu et al., 2010; Yoo, Chang, Lee, Chang, & Moon, 1997). Among the 193
vitamins found in yeast extract, niacin, pantothenic acid, riboflavin, folic acid, and 194
pyridoxine are the required B vitamins for stimulating the growth of lactobacilli 195
(Yoo et al., 1997). This bacterium was unable to grow in the medium with urea as 196
main nitrogen source, which was in agreement with the finding that the nitrogen of 197
nitrites, nitrates, or urea could not be metabolised by the Birch strain of 198
Lactobacillus (Hassinen, Durbin, Tomarelli, & Bernhart, 1951). Although the cost of 199
yeast extract is very high, its effect on cell growth is incomparable (Yoo et al., 1997); 200
inexpensive nitrogen sources with excellent effectiveness to replace yeast extract 201
remain to be found. Consequently, yeast extract was determined to be the optimal 202
nitrogen source. 203
204
3.2. Choosing the best buffer salts 205
206
LAB can metabolise carbohydrates to produce lactic acid in the process of 207
growth, which decreases the medium pH and inhibits bacterial propagation (Yáñez, 208
Marques, Gírio, & Roseiro, 2008). In this case, buffer salts in the medium can be 209
used to balance the pH and promote bacterial growth. In this study, typical buffer 210
systems at different concentrations were investigated according to the nutritional 211
requirements of LAB. As can be seen in Fig. 3, the cell growth initially increased 212
with the concentrations of buffer salts, but it then decreased with them. All of the 213
buffer salts could increase the final pH of the medium (data not shown). In addition, 214
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0.16 mol L-1 CH3COOH/CH3COONa system permitted excellent growth of the cells 215
(viable cell count was 3.26×109 cfu mL-1), and the final pH of the medium 216
containing this buffer salt (pH 4.50) was higher than that of medium without any 217
supplementation (pH 3.57). Thus 0.16 mol L-1 CH3COOH/CH3COONa was used as 218
the optimal buffer salt for the subsequent experiments. Some other reports also 219
demonstrated that the medium supplemented with proper amounts of sodium acetate 220
greatly stimulated the growth of many LAB (de Man, Rogosa, & Sharpe, 1960; Snell, 221
1945; Thorne & Kodicek, 1962). This is due to the fact that acetate acts not only as a 222
buffer, but also as a starting material for the synthesis of steroid and lipid compounds 223
that can duplicate the action of acetate when added to media sufficiently buffered 224
with phosphate (Snell, 1945). Phosphate is an important buffer and the source of 225
inorganic phosphorus, but the fast acid accumulation would soon impair growth 226
(Ledesma et al., 1977), which may be the reason for the low counts of viable cells. 227
228
3.3. Mineral requirements 229
230
Mg2+, Mn2+, Cu2+, Fe2+, and other microelements are indispensable for the 231
propagation of microorganisms, and can serve as the activator of enzyme or the 232
composition of bioactive substance (MacLeod & Snell, 1947). Fig. 4 shows the 233
effects of different microelements on the growth of L. salivarius BBE 09-18. The 234
medium containing Mn2+ showed the most significant enhancement effect on the cell 235
growth (Fig. 4a). In detail, the highest cell concentration was 3.27×109 cfu mL-1, 236
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which was 20% more than that of control, and the optimum level of MnSO4·H2O 237
was 190 mg L-1. As a constituent of lactate dehydrogenase to improve lactate 238
productivity and lactose utilisation under anaerobic conditions, manganese was 239
found to be essential for the growth of L. casei (Fitzpatrick, Ahrens, & Smith, 2001; 240
Krischke, Schröder, & Trösch, 1991; Senthuran, Senthuran, Mattiasson, & Kaul, 241
1997). Manganese supplementation could decrease the amount of yeast extract 242
required (Fitzpatrick et al., 2001), indicating that it is one of the key factors for the 243
growth of LAB. 244
Interestingly, after magnesium supplementation no significant enhancement 245
effect on the biomass of the cells was observed (Fig. 4b). This is similar to the 246
magnesium requirements of L. casei, which is at low levels if it exists (MacLeod & 247
Snell, 1947). A low concentration of copper slowly enhanced the cell concentration, 248
while it significantly inhibited the biomass at higher concentrations (Fig. 4c). As 249
copper seems to be a nonessential component for the growth of lactobacilli 250
(Bruyneel, Vande Woestyne, & Verstraete, 1989), the low demand of L. salivarius 251
BBE 09-18 for copper may be due to its specific metabolic characters. However, 252
medium containing iron hindered the propagation of the bacterium (Fig. 4d). As 253
LAB are catalase-negative and grow anaerobically without harbouring cytochrome, 254
they do not necessarily require iron as a cofactor for reproductive and redox 255
reactions, and if the requirement of iron exists, it will be only at extremely low levels 256
(Bruyneel et al., 1989; MacLeod & Snell, 1947). 257
Although many investigations have been done on the mineral requirements of 258
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LAB, the requirements may be determined by the metabolic characters and 259
physiological information of the specific bacterium (MacLeod & Snell, 1947). In 260
this study, manganese greatly promoted the growth of L. salivarius BBE 09-18, 261
while other three ions showed no significant growth-stimulating effect on the strain. 262
These findings are somewhat in disagreement with those of others. 263
264
3.4. Growth factors requirements 265
266
As LAB cannot produce the important precursors or intermediates under 267
anaerobic growth conditions (Liu et al., 2010), they require for complex growth 268
factors including several amino acids, B vitamins, purine and pyrimidine bases 269
(Fitzpatrick et al., 2001; Kitay, McNutt, & Snell, 1950; Ledesma et al., 1977; Snell, 270
1945), and unsaturated fatty acids (Kitay & Snell, 1950; Partanen, Marttinen, & 271
Alatossava, 2001). The effects of different growth factors at the concentration of 25 272
mg L-1 on the viable count of cells were investigated in this study (Fig. 5). Vitamin C, 273
guanine, uracil, and nicotinic acid had no significant stimulating effect on the cell 274
growth, while glycine and folic acid inhibited the propagation of the bacterium. This 275
may be because yeast extract already contains some B vitamins and amino acids to 276
meet the growth requirements of the cells (Yoo et al., 1997), and high concentrations 277
of these compounds inhibit the growth of the bacterium. The amounts of these B 278
vitamins present in 30 g L-1 yeast extract can be calculated (Yoo et al., 1997), thus 279
the importance and real levels of them can be determined. To better evaluate the 280
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importance of mineral requirements and growth factors, a simple medium as a 281
starting point for investigation and removal of trace impurities (as described by 282
MacLeod & Snell, 1947) will be undertaken in a further study. 283
Interestingly, Tween-80 had a very significant beneficial effect on the cell 284
growth, and the cell concentration was approximately 1.79×109 cfu mL-1. Tween-80, 285
which is a water soluble derivative of oleic acid (cis-9-octadecenoic acid), can 286
stimulate the growth of many LAB. Most LAB grown in medium containing 287
Tween-80 can incorporate oleic acid into their membranes and then transform it into 288
cyclopropane fatty acids. Cyclopropane fatty acids can act like polyunsaturated fatty 289
acids to increase the fluidity of membrane, and protect LAB from bad environmental 290
effects such as deleterious effects of oxygen, entering stationary growth phase, and 291
low pH caused by lactic acid accumulation (Partanen et al., 2001). Consequently, 292
Tween-80, which can also replace the biotin requirement of some strains, is regarded 293
as a growth-stimulating factor for LAB (Hassinen et al., 1951). As other growth 294
factors were less effective in promoting the growth of L. salivarius BBE 09-18, 295
Tween-80 was chosen as the optimal growth factor in further studies. 296
297
3.5. 2III5-2 factional factorial design 298
299
A 2III 5-2 factional factorial design (FFD) consisting of eight runs was applied 300
to identify the significant factors from the five components α-lactose, yeast extract, 301
MnSO4·H2O, CH3COONa, and Tween-80. According to the results of single-factor 302
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investigation, the coded factor levels, the real values of the five factors, and the 303
results of the response (viable count) are listed in Table 1. The linear regression 304
equation as a function of the coded values of significant factors was expressed as 305
follows: 306
307
Y1 = 9.465602 + 0.058515X1 + 0.03169X2 + 0.025162X3 + 0.009449X4 + 0.027123X5 (3) 308
309
where Y1 is the predicted response of viable count and X1, X2, X3, X4, and X5 310
represent the coded values of α-lactose, yeast extract, MnSO4·H2O, CH3COONa, and 311
Tween-80, respectively. 312
The ANOVA results showed that this model was statistically significant as 313
indicated by the low P-value (P>F, 0.0143). Both the determination coefficient 314
(R2=0.994) and the adjusted determination coefficient (adjusted R2=0.980) were high, 315
which also demonstrated the good fit and a high significance of the model. In 316
conclusion, this model could successfully predict the growth of L. salivarius BBE 317
09-18 and the coefficients obtained could be the direction ratio of the steepest ascent 318
method. As can be seen from the P-values of the five variable factors (data not 319
shown), their effects on the cell growth followed a descending order as: α-lactose, 320
yeast extract, Tween-80, CH3COONa, and MnSO4·H2O. Therefore, factors α-lactose, 321
yeast extract, and Tween-80 were chosen for further investigation. 322
323
3.6. Steepest ascent method 324
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325
The steepest ascent method was then employed to quickly reach the optimal 326
region, and its direction was determined by the coefficients of linear regression 327
model [eq. (3)] obtained in FFD. In eq. (3) the coefficients of α-lactose, yeast extract 328
and Tween-80 were all positive, which indicated that the viable count of L. salivarius 329
BBE 09-18 would increase with the concentrations of these compounds. The steepest 330
ascent experiment design and response results are presented in Table 2. The highest 331
viable count was obtained in the fourth step, but the number of living cells decreased 332
beyond this point. These results indicated that 40 g L-1 α-lactose, 50 g L-1 yeast 333
extract, and 2 mL L-1 Tween-80 had approached the neighbourhood of the optimum. 334
Therefore, the central points for the CCD were determined as follows: 40 g L-1 335
α-lactose, 50 g L-1 yeast extract, and 2 mL L-1 Tween-80. 336
337
3.7. Central composite design 338
339
A rotatable central composite design with points equidistant from the centre is 340
one of the efficient central composite designs (Ortega, Albillos, & Busto, 2003), and 341
it is applied to explore the optimal conditions for the high cell density cultivation of 342
L. salivarius BBE 09-18. To build a statistical model, we let Y represent viable cell 343
count (log10 cfu mL-1) and determined coded factor levels as follows: X1 = (α-lactose 344
– 40)/20, X2 = (yeast extract – 50)/25, and X3 = (Tween-80 – 2). The actual factor 345
levels corresponding to the coded factor levels, treatment combinations and response 346
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results are shown in Table 3. By fitting the experimental data with the least squares 347
method, a second-order polynomial regression model containing 3 linear, 3 quadratic 348
and 3 interaction terms was obtained and formulated as follows: 349
Y =9.71511 + 0.034819X1 + 0.103384X2 + 0.015094X3﹣0.052792X12 ﹣350
0.065087X22﹣0.004437X3
2 + 0.005825X1X2﹣0.00503X1X3 + 0.005508X2X3 351
(4) 352
where Y is the predicted response of viable count, and X1, X2, and X3 are the coded 353
values of the tested variables of α-lactose, yeast extract, and Tween-80, respectively. 354
The ANOVA was conducted to assess the adequacy and significance of the 355
model. The F-value (5.09) and the significant P-value (P>F, 0.009) could prove the 356
high significance and good fit of the model, respectively. Despite of the low R2 357
(0.895) and adjusted R2 (0.802), the high significance of the model could also be 358
demonstrated by the plot of predicted versus actual experimental values of viable 359
cell count (Fig. 6a). As shown in Fig. 6a, all the points clustering around the 360
diagonal line meant that this model could adequately predict the experiments. In 361
addition, the plot of the internally studentised residuals versus the predicted response 362
presented in Fig. 6b showed small residuals (<30%), indicating that this model could 363
well describe the response of bacterial growth out of the experimental region tested. 364
To understand the interaction and determine the optimum levels of the 365
variables for maximum response, the 2D contour plots and the 3D response surface 366
that are the graphical representations of the regression equation were used in this 367
study (Liu et al., 2010) (Fig. 7). The response surface of Fig. 7a represented the 368
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combination between α-lactose and yeast extract. In detail, well-defined optimum 369
variables were indicated by the convex response surface, which could also be proved 370
by the negative quadratic coefficients in Eq. (4). Furthermore, the elliptical contour 371
also demonstrated a strong interaction between α-lactose and yeast extract (data not 372
shown). Fig. 7b and Fig. 7c described the response surface of reciprocal effects to 373
the growth of L. salivarius BBE 09-18 by α-lactose and Tween-80, and yeast extract 374
and Tween-80, respectively. The optimum concentrations calculated from the 375
equation were: α-lactose = 43.8 g L-1, yeast extract = 79.5 g L-1 and Tween-80 = 5.15 376
mL L-1. Therefore, estimated optimal medium for the growth of L. salivarius BBE 377
09-18 was as follows: α-lactose 43.8 g L-1, yeast extract 79.5 g L-1, sodium acetate 378
anhydrous 13.12 g L-1, acetic acid 9.16 mL L-1, MnSO4·H2O 190 mg L-1 and 379
Tween-80 5.15 mL L-1. And the estimated maximum response corresponding to the 380
optimum factor levels was 6.01×109 cfu mL-1. Verification experiments were 381
performed with L. salivarius BBE 09-18 grown in estimated optimal medium for 18 382
h at 37 °C. The actual cell concentration was 5.94×109 cfu mL-1, which was nearly 383
three times higher than that in standard MRS medium. 384
At present, the high cell density culture of LAB is centred on reducing the 385
growth inhibition caused by lactic acid accumulation (Schiraldi et al., 2003). There 386
have been several methods to achieve this aim. In this research, we used buffer salts 387
to prevent the pH from lowering, and obtained a viable cell count of 5.94×109 cfu 388
mL-1, which was better than fed-batch fermentation (the final cell concentration was 389
4.7 g L-1, about 5.62×109 cfu mL-1; Zhang, Cong, & Shi, 2010) and immobilisation 390
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of Bifidobacterium longum in gellan gum gel beads (the highest cell concentration 391
was 4.9×109 cfu mL-1; Doleyres, Paquin, LeRoy, & Lacroix, 2002). We also 392
combined several optimisation methods and optimised the medium compositions 393
based on the specific metabolic characters and nutritional requirements of L. 394
salivarius BBE 09-18, which was more effective than only using RSM (Liew et al., 395
2005; Lim et al., 2007) (final cell concentrations obtained were 2.75×109 and 396
3.2×109 cfu mL-1, respectively). Although much work has to be carried out for the 397
high concentration cultivation of L. salivarius BBE 09-18, this optimised medium 398
can be used as a basal medium for the high cell density culture studies of L. 399
salivarius BBE 09-18 and the production of high effective starter concentrates. 400
401
4. Conclusions 402
403
According to the metabolic characters and physiological information of L. 404
salivarius BBE 09-18, the combinations of “change one factor at a time” method, 405
factional factorial design, steepest ascent method and central composite design were 406
used to determine optimal medium compositions for the high cell density cultivation 407
of this bacterium. This study demonstrated that RSM was useful in designing, 408
analysing, searching for the optimum points and evaluating the effects of factors 409
leading to a higher cell concentration of L. salivarius BBE 09-18. Through the 410
verification experiment, we ascertained that the optimised medium gave higher 411
counts of viable cells than the standard MRS medium. This will help to produce high 412
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cell density cultures of L. salivarius BBE 09-18, high effective starter concentrates 413
and probiotic ingredients in the dairy industry. 414
415
Acknowledgements 416
417
This work was financially supported by the Key Program of National Natural 418
Science Foundation of China (No. 20836003), the National Natural Science 419
Foundation of China (No. 30900013), the National High Technology Research and 420
Development Program of China (863 Program, 2011AA100901), the National Key 421
Technology R&D Program of China (2011BAK10B03), and the Priority Academic 422
Program Development of Jiangsu Higher Education Institutions. 423
424
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Figure legends
Fig. 1. Effects of different carbon sources (Gal, D(+)-galactose; Mlt, maltose; Fru, D-fructose;
Glu, glucose; Suc, sucrose; Lac, α-lactose; Sta, starch; Dex, dextrin; Xyl, xylose) at a
concentration of 2% (w/v) on the growth of L. salivarius BBE 09-18. Results are the mean
values of three replicates, and the error bars indicate standard deviations.
Fig. 2. Effects of 2% (w/v) of different nitrogen sources (PS, peptone, soya; Pep, peptone;
Try, tryptone; YE, yeast extract; BE, beef extract; AS, ammonium sulphate; SN, sodium
nitrate; U, urea) on the cell concentration of L. salivarius BBE 09-18.
Fig. 3. Effects of different buffer systems (�, HAc/NaAc; , NaH2PO4/Na2HPO4; ,
KH2PO4/Na2HPO4) at different concentrations (0.00-0.24 mol L-1) on the propagation of L.
salivarius BBE 09-18.
Fig. 4. Effects of different microelements on the viable count of L. salivarius BBE 09-18: a,
MnSO4·H2O (0-200 mg L-1); b, MgSO4 (0-800 mg L-1); c, CuSO4 (0-40 mg L-1); d,
FeSO4·7H2O (0-100 mg L-1).
Fig. 5. Effects of different growth factors (C, control; VitC, vitamin C; Gua, guanine; Ur,
uracil; NA, nicotinic acid; FA, folic acid; T80, tween 80) at 25 mg L-1 on the cell density of L.
salivarius BBE 09-18.
Fig. 6. Diagnostics of Eq. (4): (a) predicted values versus actual experimental values of
viable bacterium count and (b) plot of the residuals versus predicted values of viable count.
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Fig. 7. Response surfaces for the effects of: a, α-lactose and yeast extract on the cell
concentration of L. salivarius BBE 09-18 with Tween-80 at 2.0 mL L-1; b, α-lactose and
Tween-80 on the growth of L. salivarius BBE 09-18 with yeast extract at 50.0 g L-1; c, yeast
extract and Tween-80 on the growth of L. salivarius BBE 09-18 with α-lactose at 40.0 g L-1.
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Table 1
2III5-2 factorial design matrix and results of the dependent variable viable count.
Factors and levels a Run X1 (g L-1) X2 (g L-1) X3 (g L-1) X4 (g L-1) X5 (mL L-1)
Y (log10 cfu mL-1)
1 -1 (10) -1 (20) -1 (6.56) 1 (0.19) 1 (1.25) 9.390 2 1 (30) -1 (20) -1 (6.56) -1 (0.15) -1 (0.75) 9.438 3 -1 (10) 1 (40) -1 (6.56) -1 (0.15) 1 (1.25) 9.428 4 1 (30) 1 (40) -1 (6.56) 1 (0.19) -1 (0.75) 9.525 5 -1 (10) -1 (20) 1 (13.12) 1 (0.19) -1 (0.75) 9.379 6 1 (30) -1 (20) 1 (13.12) -1 (0.15) 1 (1.25) 9.528 7 -1 (10) 1 (40) 1 (13.12) -1 (0.15) -1 (0.75) 9.431 8 1 (30) 1 (40) 1 (13.12) 1 (0.19) 1 (1.25) 9.625 a -1 and 1 are coded levels.
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Table 2
Results of the steepest ascent path experiments.
Steps α-lactose (g L-1)
Yeast extract (g L-1)
Tween-80 (mL L-1)
Viable count (log10 cfu mL-1)
Origin 20 30 1 9.605 � 5 5 0.25 Origin+� 25 35 1.25 9.613 Origin+2� 30 40 1.50 9.615 Origin+3� 35 45 1.75 9.622 Origin+4� 40 50 2.00 9.626 Origin+5� 45 55 2.25 9.624
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Table 3
Treatment combinations and responses of central composite design.
Factors and levels a Run X1 α-lactose (g L-1)
X2 Yeast extract (g L-1)
X3 Tween-80 (mL L-1)
Y response b
(log10 cfu mL-1)
1 -1 (20) -1 (25) -1 (1) 9.556 2 -1 (20) -1 (25) 1 (3) 9.568 3 -1 (20) 1 (75) -1 (1) 9.663 4 -1 (20) 1 (75) 1 (3) 9.713 5 1 (60) -1 (25) -1 (1) 9.563 6 1 (60) -1 (25) 1 (3) 9.571 7 1 (60) 1 (75) -1 (1) 9.709 8 1 (60) 1 (75) 1 (3) 9.723 9 -1.682 (6.36) 0 (50) 0 (2) 9.400 10 1.682
(73.64) 0 (50) 0 (2) 9.643
11 0 (40) -1.682 (7.96) 0 (2) 9.230 12 0 (40) 1.682 (92.04) 0 (2) 9.743 13 0 (40) 0 (50) -1.682 (0.32) 9.647 14 0 (40) 0 (50) 1.682 (3.68) 9.719 15 0 (40) 0 (50) 0 (2) 9.714 16 0 (40) 0 (50) 0 (2) 9.719 17 0 (40) 0 (50) 0 (2) 9.717 18 0 (40) 0 (50) 0 (2) 9.716 19 0 (40) 0 (50) 0 (2) 9.721 20 0 (40) 0 (50) 0 (2) 9.719
a -1.682, -1, 0, 1 and 1.682 are coded levels.
b Viable count of L. salivarius BBE 09-18, and the results are the average of three replicates.
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D(+)-Galactose
Maltose
D-Fructose
Glucose
Sucrose
α-Lactose
StarchDextrin
Xylose7.50
8.00
8.50
9.00
9.50
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
1
Fig. 1 2
Gal Mlt Fru Glu Suc Lac Sta Dex Xyl
Via
ble
coun
t (lo
g 10 cf
u m
L-1
)
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2
Peptone,soyaPeptone
Tryptone
Yeast extract
Beef extract
Ammonium sulfate
Sodium nitrate Urea
0.00
2.00
4.00
6.00
8.00
10.00
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
3
Fig. 2 4
Via
ble
coun
t (lo
g 10 cf
u m
L-1
)
PS Pep Try YE BE AS SN U
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0.00 0.04 0.08 0.12 0.16 0.20 0.248.75
9.00
9.25
9.50
9.75
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
Concentration (mol L-1)
HAc/NaAc NaH
2PO
4/Na
2HPO
4
KH2PO
4/Na
2HPO
4
5
Fig. 3 6
Via
ble
coun
t (lo
g 10 cf
u m
L-1
)
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0 50 100 150 2009.10
9.20
9.30
9.40
9.50
9.60
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
MnSO4 H
2O (mg L-1).
a
0 200 400 600 800
9.10
9.20
9.30
9.40
9.50
9.60
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
MgSO4 (mg L-1)
b
7
0 10 20 30 409.10
9.20
9.30
9.40
9.50
9.60
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
CuSO4 (mg L-1)
c
0 20 40 60 80 100
9.10
9.20
9.30
9.40
9.50
9.60
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
FeSO4 7H
2O (mg L-1).
d
8
Fig. 4 9
10
11
12
13
Via
ble
coun
t (lo
g 10 cf
u m
L-1
) V
iabl
e co
unt (
log 1
0 cf
u m
L-1
)
Via
ble
coun
t (lo
g 10 cf
u m
L-1
) V
iabl
e co
unt (
log 1
0 cf
u m
L-1
) a b
c d
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Control
Vitamin CGuanine
Uracil
Nicotinic acidGlycine
Folic acid
Tween-808.50
8.75
9.00
9.25
9.50
Via
ble
coun
t (lo
g 10 C
FU
mL-1
)
14
Fig. 5 15
16
17
18
19
20
21
22
23
24
25
26
27
28
Via
ble
coun
t (lo
g 10 cf
u m
L-1
)
C VitC Gua Ur NA Gly FA T80
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29
Fig. 6 30
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31
Fig. 7 32
33
Via
ble
coun
t (l
og10
cfu
mL
-1)
Via
ble
coun
t (l
og10
cfu
mL
-1)
Via
ble
coun
t (l
og10
cfu
mL
-1)