Effect of inoculum composition and low KCl supplementation on the biological and rheological stability of an immobilized-cell system for mixed mesophilic lactic starter production.

Two strains of Lactococcus lactis subsp. lactis (L. lactis KB and KBP) and one of L. lactis subsp. lactis biovar. diacetylactis (L. diacetylactis MD) were immobilized separately in kappa-carrageenan-locust bean gum gel beads. Continuous fermentations were carried out in supplemented whey permeate in a 1-L pH-controlled stirred tank reactor inoculated with a 30% (v/v) bead inoculum and a bead ratio of 55:30:15 for KB, KBP, and MD, respectively. The process demonstrated a high productivity and microbial stability during the 7-week continuous culture. Compared with previous experiments carried out with an inoculum bead ratio of 33:33:33 for KB, KBP, and MD beads, respectively, the modification of the inoculum bead ratio had apparently little effect on free and immobilized, total and specific populations. A dominant behavior of L. diacetylactis MD over the other strains of the mixed culture was observed both with free-cell populations in the effluent and with immobilized-cell populations. Additional experiments were carried out with other strain combinations for continuous inoculation-prefermentation of milk. The data also confirmed the dominance of L. diacetylactis during long-term continuous immobilized-cell fermentations. This dominance may be tentatively explained by the local competition involved in the development of the bead cross-contamination and in citrate utilization by L. diacetylactis strains. The gel beads demonstrated a high rheological stability during the 7-week continuous fermentation even at low KCl supplementation of the broth medium (25 mM KCl).     

Quantitative determination of the spatial distribution of pure- and mixed-strain immobilized cells in gel beads by immunofluorescence

A new method was developed to detect and quantify two strains, Lactococcus lactis subsp. lactis biovar. diacetylactis MD and Bifidobacterium longum ATCC 15707, immobilized separately and co-immobilized in gel beads, using specific polyclonal antibodies and confocal laser-scanning microscopy. The establishment of biomass concentration profiles for each strain was measured during colonization of beads using successive pH-controlled batch fermentations. Growth occurred preferentially in 200- and 300-microm peripheral layers of the beads for L. diacetylactis and B. longum, respectively. Repeated-batch cultures with immobilized cells permitted the production of a mixed culture containing a non-competitive strain of bifidobacteria, as a result of immobilized-cell growth and high cell-release activity from the beads. During co-immobilized fermentations, there were no apparent interactions between the strains.     

Increased stress tolerance of Bifidobacterium longum and Lactococcus lactis produced during continuous mixed-strain immobilized-cell fermentation

AIMS: The effect of immobilization and long-term continuous culture was studied on probiotic and technological characteristics of lactic acid and probiotic bacteria. METHODS AND RESULTS: A continuous culture in a two-stage system was carried out for 17 days at different temperatures ranging from 32 to 37 degrees C, with a first reactor containing Bifidobacterium longum ATCC 15707 and Lactococcus lactis subsp. lactis biovar. diacetylactis MD immobilized separately in gel beads, and a second reactor operated with free cells released from the first reactor. The tolerance of free cells from both strains produced in the effluent medium of both reactors to hydrogen peroxide, simulated gastric and intestinal juices, antibiotics and nisin, and freeze-drying markedly increased with culture time and was generally higher after 6 days than that of stationary-phase cells produced during free-cell batch fermentations. The reversibility of the acquired tolerance of B. longum, but not L. diacetylactis, to antibiotics was shown during successive free-cell batch cultures. CONCLUSIONS: Free cells produced from continuous immobilized-cell culture exhibited altered physiology and increased tolerance to various chemical and physico-chemical stresses. SIGNIFICANCE AND IMPACT OF THE STUDY: Continuous culture with immobilized cells could be used to produce probiotic and lactic acid bacteria with enhanced technological and probiotic characteristics.     

Continuous mixed strain mesophilic lactic starter production in supplemented whey permeate medium using immobilized cell technology

The aim of this work was to study a new process for the continuous production of mixed-strain lactic acid bacteria starters using immobilized cells. Three strains of Lactococcus (two Lactococcus lactis subsp. lactis: KB and KBP, and one Lactococcus lactis subsp. lactis biovar diacetylactis: MD) were immobilized separately in kappa-carrageenan-locust bean gum gel beads. Continuous fermentations were carried out in a 1 L pH-controlled stirred tank reactor with a 30% (v/v) bead inoculum (strain ratio 1:1:1), continuously fed with a whey UF permeate medium, supplemented with 1.5% yeast extract and 0.1M KCl. The effects of three parameters-pH, temperature (T), dilution rate (D), and their interactions on the composition and activity of the culture in the effluent at pseudosteady state were studied according to a rotatable central composite design, during a 53-day fermentation. The process showed a high biological stability and no strain became dominant, or was eliminated from the bioreactor. The statistical analysis showed that the three strains were differently affected by the studied parameters, and that a large range of effluent starter composition can be achieved by varying D, pH, and T. However, the acidifying characteristics were not affected by the culture conditions. A cross-contamination from other strains of the mixed culture was observed in gel beads entrapping a pure culture at the fermentation onset, and led to a biomass redistribution within the beads. However, the strain ratio (KB:KBP:MD) observed after the 53-day experiment (1:2:2) was close to the initial bead ratio (1:1:1). The beads demonstrated a high mechanical stability throughout the 53-day continuous fermentation. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 502-516, 1997.     

pH-controlled cell release and biomass distribution of alginate-immobilized Lactococcus lactis subsp. lactis

AIMS: To investigate the growth and release of Lactococcus lactis subsp. lactis in gel beads and to affect rates of cell release by changing the growth conditions. METHODS AND RESULTS: The rate of release and the distribution of immobilized L. lactis subsp. lactis in alginate beads were studied in continuous fermentations for 48 h. A change in operating pH from 6.5 to 9.25 initially reduced the ratio of the rates of cell release to lactate production by almost a factor of 105. Compared with fermentations at pH 6.5, growth at pH 9.25 also increased the final internal bead biomass concentration by a factor of 5 and increased the final rate of lactate production by 25%. After 48 h, the ratio of the rates of cell release to lactate production was still 10 times lower than in fermentations at pH 6.5. CONCLUSIONS: A change in the operating pH from 6.5 to 9.25 reduced rates of cell release throughout 48 h of fermentation and increased the final rates of lactate production and internal bead biomass concentration. SIGNIFICANCE AND IMPACT OF THE STUDY: These data illustrate that diffusional limitations and corresponding pH gradients can be exploited in affecting the distribution of immobilized growing cells and their concomitant release.     

Employment of stressful conditions during culture production to enhance subsequent cold- and acid-tolerance of bifidobacteria

AIMS: This study examined whether exposure of early stationary phase Bifidobacterium longum and B. lactis cells to various combinations of reduced temperature, reduced pH and starvation would enhance the cells' subsequent cold- and/or acid-tolerance. METHODS AND RESULTS: Survival of B. longum in growth medium at 6 degrees C significantly (P < 0.05) increased as a result of starving cells for 30 or 60 min without any simultaneous decrease in temperature or pH. Acid-tolerance of B. lactis (at pH 3.5 in synthetic gastric fluid) increased significantly when the growth medium pH was decreased from 6.0 to 5.2 and cells experienced 30 or 60 min of starvation. Enhanced B. lactis acid-tolerance persisted through 8-11 weeks of -80 degrees C storage in the pH 5.2 growth medium. Upon addition to milk during yogurt manufacture, these cells initially had enhanced acid-tolerance relative to untreated cells but untreated cells became equally acid-tolerant during the first 2.5 h of yogurt manufacture. CONCLUSIONS: The cold- and acid-tolerance of bifidobacteria vary widely, but may be significantly increased by application of sub-lethal stress to early stationary phase cells during culture production. SIGNIFICANCE AND IMPACT OF THE STUDY: The enhancement of B. lactis acid-tolerance observed in this study may be of potential importance in the production of effective ready-to-consume probiotic dietary supplements.     

Novel method for cell immobilization and its application for production of oligosaccharides from sucrose

AIMS: The purpose of the present investigation was to develop a novel method for cell immobilization. METHODS AND RESULTS: Aureobasidium pullulans cells were mixed with an alginate solution, and the mixture was extruded to form small gel beads as hydrated-immobilized cells. The beads were then placed at -15 degrees C for 6-24 h to induce freeze-dehydration. The freeze-dehydration resulted in shrinkage of beads as a result of water removal reducing bead volume by 82% and bead weight by 85%. The dehydrated beads were successfully used for the production of fructo-oligosaccharides in a model reactor system. CONCLUSIONS: Dehydrated beads may provide some commercial advantages over conventional immobilized cells. SIGNIFICANCE AND IMPACT OF THE STUDY: This study shows that bioreactor performance can be improved up to two times by the use of the dehydrated beads.     

Development of a cell-loaded biosupport separator for continuous immobilized-cell perfusion culture

An efficient cell-loaded biosupport separator of the decantor type was developed and applied for a continuous perfusion culture to produce cyclosporin A (CyA), in which fungal cells were immobilized on Celite beads. In the preliminary experiments employing highly viscous polymer (carboxymethyl cellulose) solutions, the decantor showed good separation performances at high solution viscosites and dilution rates. Two concentric cylindrical tubes installed inside the decantor turned out to play key roles in the efficient separation of the immobilized cells. By installing the decantor on an immobilized-cell perfusion bioprocess system, a stable continuous operation was possible even at a high dilution rate for an extended period, leading to high productivities of free cells and CyA. Almost no immobilized biomass existed in the effluent stream from the bioreactor, demonstrating the effectiveness of the decantor system. It is noteworthy that we could obtain these results despite unfavorable fermentation conditions, i.e., reduced apparent density of cell-loaded beads and increased drag force on the bead particles caused by overgrowth of cells on the bead surface, tubulence caused by large air bubbles, and the existence of a high density of suspended fungal cells (10 g/L) in the fermentation broth.     

Production of dextransucrase by Leuconostoc mesenteroides immobilized in calcium-alginate beads: I. Batch and fed-batch fermentations

In batch fermentation Leuconostoc mesenteroides immobilized in calcium alginate beads produced a total dextransucrase activity equal to about 93% of that by free, suspended bacterial cells under comparable conditions in a bubble column reactor. Continuous sucrose feeding (5 g/L h) to the immobilized-cell culture in the airlift bioreactor increased production of enzymatic activity by about 107% compared with ordinary batch operation of this reactor. About 14% of the enzymatic activity produced by the immobilized cells appears as soluble activity in the cell-free broth compared with about 40% in case of free cells. In an airlift bioreactor, both the soluble and the intact (sorbed and entrapped) enzymatic activity produced by the immobilized bacterial cells was about 34% greater under automatic pH control, compared to that produced in a bubble column reactor with only manual pH control. During formation of dextran by intact enzyme within cells and beads, declines are observed in apparent enzymatic activity.     

Removal of hydrogen sulfide by Chlorobium thiosulfatophilum in immobilized-cell and sulfur-settling free-cell recycle reactors.

Bioconversion of hydrogen sulfide to elementary sulfur by the photosynthetic bacterium Chlorobium thiosulfatophilum was studied in immobilized-cell and sulfur-settling free-cell recycle reactors. The cells immobilized in strontium alginate beads excreted elementary sulfur and accumulated it as crystal in the bead matrices, which made it possible that the reactor broth remained clear and the light penetrated the reactor deeper than with the free cells. In comparison with the free cells, the immobilized cells required 30% less light energy at a H2S removal rate of 2 mM/(L.h) and showed an activity of 2.4 times that of the free cells. However, in 40 h after the reaction the deterioration of the H2S removal efficiency became significant due to the accumulation of sulfur in the beads. The scanning electron micrograph (SEM) and energy-dispersive X-ray spectrometer (EDS) studies showed that the sulfur in the beads existed within a layer of 0.4 mm from the bead surface. In the sulfur-settling free-cell recycle reactor, about 80% of the sulfur excreted by the free cells could be removed in a settler. The 4-L fed batch reactor with the settler improved the light transmission to result in a H2S removal rate of 3 mumol/(mg of protein.h), 50% higher than that without it. The settling recycle reactor was much better in the removal of H2S than the immobilized-cell reactor because the former was a continuous system with the constant removal of sulfur particles by settling and of spent medium by supplying fresh medium at the same rate as the filtering rate of the reactor broth, while the latter was essentially a batch system where toxic metabolites and produced sulfur could not be removed.     

Citrate Fermentation by Lactococcus and Leuconostoc spp

Citrate and lactose fermentation are subject to the same metabolic regulation. In both processes, pyruvate is the key intermediate. Lactococcus lactis subsp. lactis biovar diacetylactis homofermentatively converted pyruvate to lactate at high dilution (growth) rates, low pH, and high lactose concentrations. Mixed-acid fermentation with formate, ethanol, and acetate as products was observed under conditions of lactose limitation in continuous culture at pH values above 6.0. An acetoin/butanediol fermentation with alpha-acetolactate as an intermediate was found upon mild aeration in continuous culture and under conditions of excess pyruvate production from citrate. Leuconostoc spp. showed a limited metabolic flexibility. A typical heterofermentative conversion of lactose was observed under all conditions in both continuous and batch cultures. The pyruvate produced from either lactose or citrate was converted to d-lactate. Citrate utilization was pH dependent in both L. lactis and Leuconostoc spp., with maximum rates observed between pH 5.5 and 6.0. The maximum specific growth rate was slightly stimulated by citrate, in L. lactis and greatly stimulated by citrate in Leuconostoc spp., and the conversion of citrate resulted in increased growth yields on lactose for both L. lactis and Leuconostoc spp. This indicates that energy is conserved during the metabolism of citrate.     

Measurement of phagocytosis using fluorescent latex beads

Fluorescent monodisperse latex beads and a computer-centered spectrofluorimeter were used to devise a sensitive new assay for phagocytosis. LM fibroblasts, a transformed cell line with a high endocytic rate, were exposed to fluoresbrite beads and the following parameters were investigated: incubation time, incubation temperature and bead/cell ratio. The bead uptake was linear for 60 min over a wide range of bead/cell ratios up to 130 beads/cell. Phagocytosis was inhibited at 4 degrees C, by incubation in the presence of colchicine, and by glucose deprivation. Scanning and transmission electron microscopy were used to confirm that at 37 degrees C both bead adsorption and internalization occurred while at 4 degrees C only bead adsorption but not endocytosis occurred. Large bead sizes (0.86 and 1.72 micrometer diameter) were most useful due to higher fluorescence and higher signal to noise ratios than smaller beads (0.25 and 0.57 micrometer diameter). Beads (0.86 micrometer diameter) were taken up at a rate of 4.4 beads/cell/h at 37 degrees C when a bead/cell ratio of 70 was used. The uptake was zero when assayed at zero time. These criteria establish that fluoresbrite beads provide a useful new fluorimetric assay for phagocytosis.     

Bifidobacterium longum ATCC 15707 cell production during free- and immobilized-cell cultures in MRS-whey permeate medium

Bifidobacterium longum ATCC 15707 cell production was studied in MRS medium supplemented with whey permeate (MRS-WP) during free-cell batch fermentations and continuous immobilized-cell cultures. Very high populations were measured after 12 h batch cultures in MRS-WP medium controlled at pH 5.5 (1.7+/-0.5x10(10) cfu/ml), approximately 2-fold higher than in non-supplemented MRS. Our study showed that WP is a low-cost source of lactose and other components that can be used to increase bifidobacteria cell production in MRS medium. Continuous fermentation in MRS-WP of B. longum immobilized in gellan gum gel beads produced the highest cell concentrations in the effluent (4.9+/-0.9x10(9) cfu/ml) at a dilution rate (D) of 0.5 h(-1). However, maximal volumetric productivity (6.9+/-0.4x10(9) cfu ml(-1)h(-1)) during continuous cultures was obtained at D =2.0 h(-1), and was approximately 9.5-fold higher than during free-cell batch cultures at an optimal pH of 5.5 (7.2x10(8) cfu ml(-1)h(-1)).     

Media and process parameters affecting the growth, strain ratios and specific acidifying activities of a mixed lactic starter containing aroma-producing and probiotic strains

AIMS: The effects of medium-composition and fermentation parameters on the properties of mixed mesophilic starters were studied. The starter was composed of Lactococcus lactis ssp. lactis (L. lactis), Lactococcus lactis ssp. cremoris (L. cremoris), Lactobacillus rhamnosus (Lact. rhamnosus) and Leuconostoc mesenteroides ssp. cremoris (Leuc. cremoris). METHODS AND RESULTS: The media used were reconstituted skim milk (RSM), and whey-based media with either citrate or phosphate buffers. The fermentation parameters were incubation temperature (22 degrees C or 32 degrees C), no pH control, and pH control in pH zones of either pH 6.0-5.8 or pH 6.0-5.2. The starter properties were strain ratio, specific acidifying activity (SAA), total population, residual carbohydrates and organic acids produced. The growth of L. lactis was favoured under pH control in whey-based media. High concentrations of Lact. rhamnosus were favoured in whey-based media prepared at 32 degrees C. The highest contents of Leuc. cremoris were obtained in starters prepared in RSM at 22 degrees C without pH control. Starters prepared under pH control gave the highest populations and made it possible for significantly lower inoculation rates (IR) to be used to carry out subsequent milk fermentations. However, the SAA of starters prepared under pH control were lower than the SAA of starters grown without any pH control. CONCLUSIONS: None of the conditions enabled the strain ratio at inoculation to be maintained. The data show that it is possible to prepare a mesophilic starter that has a significant probiotic Lact. rhamnosus content; this starter could be used in the preparation of probiotic-containing cheeses or in Leuc. cremoris for aroma production in fermented milks. SIGNIFICANCE AND IMPACT OF THE STUDY: This study provides data on what should be expected with respect to strain ratios and IR if cheesemakers decide to shift their aroma-producing starter production method from the traditional 'milk-based without pH control' method to whey-based media used with pH-zone control strategies.     

固定化乳酸乳球菌连续生产Nisin的研究

以海藻酸钙为材料 ,固定乳酸乳球菌 (Lactococcuslactissubsp .lactis)SM5 2 6 ,研究不同条件对Nisin合成的影响。结果表明 ,利用 2 %海藻酸钠在 1 0mmol LCaCl2 条件下 ,得到的固定化细胞颗粒稳定性较好 ,可维持 90h无破裂 ;在发酵过程中SYS3培养基中的无机盐成分尤其磷酸盐对固定化颗粒有破坏作用 ;用mSYS3培养基代替SYS3 ,通过 72h三批次循环的半连续培养 ,Nisin活性为 85 0IU mL ,无明显的细胞渗漏现象。连续化生产 70h ,Nisin活性达 1 1 5 0IU mL ,相当于游离细胞的发酵水平。     

Sugar Utilization and Acid Production by Free and Entrapped Cells of Streptococcus salivarius subsp. thermophilus, Lactobacillus delbrueckii subsp. bulgaricus, and Lactococcus lactis subsp. lactis in a Whey Permeate Medium

Cells of Streptococcus salivarius subsp. thermophilus and Lactococcus lactis subsp. lactis entrapped in k-carrageenan-locust bean gum gel performed similarly to free cells in the conversion of lactose to lactic acid. Bead diameter influenced the fermentation rate. Cells entrapped in smaller beads (0.5 to 1.0 mm) showed higher release rates, higher lactose, glucose, and formic acid utilization, higher galactose accumulation, and higher lactic acid production than did cells entrapped in larger beads (1.0 to 2.0 mm). Values for smaller beads were comparable with those for free cells. Immobilization affected the fermentation rate of lactic acid bacteria, especially Lactobacillus delbrueckii subsp. bulgaricus. Entrapped cells of L. delbrueckii subsp. bulgaricus demonstrated a lower lactic acid production than did free cells in batch fermentation. The kinetics of the production of formic and pyruvic acids by L. lactis subsp. lactis and S. salivarius subsp. thermophilus are presented.     

Cloning of the citrate permease gene of Lactococcus lactis subsp. lactis biovar diacetylactis and expression in Escherichia coli.

The citrate plasmid (Cit+ plasmid) from Lactococcus lactis subsp. lactis biovar diacetylactis was cloned into the EcoRI site of plasmid pUC18. This recombinant plasmid enabled Escherichia coli K-12 to transport and utilize citrate as a source of energy, indicating expression of the citrate permease from L. lactis biovar diacetylactis. The citrate permease was under the control of the lac promoter of pUC18. Genetic expression of the Cit+ plasmid in maxicells revealed that the plasmid encoded two polypeptides of 47 and 32 kilodaltons, determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis.     

Cloning of the citrate permease gene of Lactococcus lactis subsp. lactis biovar diacetylactis and expression in Escherichia coli

The citrate plasmid (Cit+ plasmid) from Lactococcus lactis subsp. lactis biovar diacetylactis was cloned into the EcoRI site of plasmid pUC18. This recombinant plasmid enabled Escherichia coli K-12 to transport and utilize citrate as a source of energy, indicating expression of the citrate permease from L. lactis biovar diacetylactis. The citrate permease was under the control of the lac promoter of pUC18. Genetic expression of the Cit+ plasmid in maxicells revealed that the plasmid encoded two polypeptides of 47 and 32 kilodaltons, determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis.     

Acetic acid production from lactose by an anaerobic thermophilic coculture immobilized in a fibrous-bed bioreactor

An anaerobic thermophilic coculture consisting of a heterofermentative bacterium (Clostridium thermolacticum) and a homoacetogen (Moorella thermoautotrophica) was developed for acetic acid production from lactose and milk permeate. The fermentation kinetics with free cells in conventional fermentors and immobilized cells in a recycle batch fibrous-bed bioreactor were studied. The optimal conditions for the cocultured fermentation were found to be 58 degrees C and pH 6.4. In the free-cell fermentation, C. thermolacticum converted lactose to acetate, ethanol, lactate, H(2) and CO(2), and the homoacetogen then converted lactate, H(2), and CO(2) to acetate. The overall acetate yield from lactose ranged from 0.46 to 0.65 g/g lactose fermented, depending on the fermentation conditions. In contrast, no ethanol was produced in the immobilized-cell fermentation, and the overall acetate yield from lactose increased to 0.8-0.96 g/g lactose fermented. The fibrous-bed bioreactor also gave a higher final acetate concentration (up to 25. 5 g/L) and reactor productivity (0.18-0.54 g/L/h) as compared to those from the free-cell fermentation (final acetate concentration, 15 g/L; productivity, 0.06-0.08 g/L/h). The superior performance of the fibrous-bed bioreactor was attributed to the high cell density (20 g/L) immobilized in the fibrous-bed and adaptation of C. thermolacticum cells to tolerate a higher acetate concentration. The effects of yeast extract and trypticase as nutrient supplements on the fermentation were also studied. For the free-cell fermentation, nutrient supplementation was necessary for the bacteria to grow in milk permeate. For the immobilized-cell fermentation, plain milk permeate gave a high acetate yield (0.96 g/g), although the reactor productivity was lower than those with nutrient supplementation. Balanced growth and fermentation activities between the two bacteria in the coculture are important to the quantitative conversion of lactose to acetic acid. Lactate and hydrogen produced by C. thermolacticum must be timely converted to acetic acid by the homoacetogen to avoid inhibition by these metabolites.     

Cloning and partial characterization of regulated promoters from Lactococcus lactis Tn917-lacZ integrants with the new promoter probe vector, pAK80.

Transposon Tn917-LTV1 was used to produce a collection of Lactococcus lactis strains with fusion of a promoterless lacZ gene to chromosomal loci. Screening 2,500 Tn917-LTV1 integrants revealed 222 that express beta-galactosidase on plates at 30 degrees C. Pulsed-field gel electrophoresis revealed Tn917-LTV1 insertions in at least 13 loci in 15 strains analyzed. Integrants in which beta-galactosidase expression was regulated by temperature or pH and/or arginine concentration were isolated. In most cases, the regulation observed on plates was reproducible in liquid medium. One integrant, PA170, produces beta-galactosidase at pH 5.2 but not at pH 7.0, produces more beta-galactosidase at 15 degrees C than at 30 degrees C, and has increased beta-galactosidase activity in the stationary phase. DNA fragments potentially carrying promoters from selected Lactococcus lactis integrants were cloned in Escherichia coli. A new promoter probe vector, pAK80, containing promoterless beta-galactosidase genes from Leuconostoc mesenteroides subsp. cremoris and the Lactococcus lactis subsp. lactis biovar diacetylactis citrate plasmid replication region was constructed, and the lactococcal fragments were inserted. Plasmid pAK80 was capable of detecting and discriminating even weak promoters in Lactococcus lactis. When inserted in pAK80, the promoter cloned from PA170 displayed a regulated expression of beta-galactosidase analogous to the regulation observed in PA170.