Production of nisin with continuous adsorption to Amberlite XAD-4 resin using<Emphasis Type="Italic"> Lactococcus lactis</Emphasis> N8 and<Emphasis Type="Italic"> L. lactis</Emphasis> LAC48

The production of nisin, biomass and lactic acid in pH-controlled and uncontrolled batch fermentation and batch fermentation (pH 5.5) with continuous removal of nisin was examined in the parent strain Lactococcus lactis N8 and LAC48. Strain LAC48 in batch fermentor (pH not controlled) gave a maximum nisin concentration of 2.5×10⁶ IU g dcw^–1. The nisin concentration remained high (2.0×10⁶ IU g dcw^–1) after the logarithmic growth phase (10–22 h), whereas nisin production of strain N8 decreased after the logarithmic growth phase. The maximum nisin production of strain LAC48 was not directly related to the biomass formation and not associated with growth. In order to study end product inhibition in nisin production, a system was built for adsorption of nisin during fermentation. The adsorbent Amberlite XAD-4 was found to have an effective binding capacity for nisin. Cells of LAC48 and N8 compensated for the removal of nisin, indicating that nisin production also occurs in the stationary phase.     

Continuous nisin production with bioengineered <Emphasis Type="Italic">Lactococcus lactis</Emphasis> strains

Nisin production in continuous cultures of bioengineered Lactococcus lactis strains that incorporate additional immunity and regulation genes was studied. Highest nisin activities were observed at 0.2 h^–1 dilution rate and 12.5 g l^–1 fructose concentration for all strains. Recombinant strains were able to produce greater amounts of nisin at dilution rates below 0.3 h⁻¹ compared to the control strain. However, this significant difference disappeared at dilution rates of 0.4 and 0.5 h^–1. For the strains LL27, LAC338, LAC339, and LAC340, optimum conditions for nisin production were determined to be at 0.29, 0.26, 0.27, and 0.27 h^–1 dilution rates and 11.95, 12.01, 11.63, and 12.50 g l^–1 fructose concentrations, respectively. The highest nisin productivity, 496 IU ml^–1 h^–1, was achieved with LAC339. The results of this study suggest that low dilution rates stabilize the high specific nisin productivity of the bioengineered strains in continuous fermentation. Moreover, response surface methodology analysis showed that regulation genes yielded high nisin productivity at wide ranges of dilution rates and fructose concentrations.     

Thermostable cellulases from <Emphasis Type="Italic">Streptomyces</Emphasis>sp.: scale-up production in a 50-l fermenter

Thermostable cellulase was produced by Streptomyces sp. T3-1 grown in a 50-l fermenter. Maximum cellulase activity was attained on the fourth day when agitation speeds and aeration rates were controlled at 300 rpm and 0.75 vvm, respectively. Maximum enzyme activities were: 148 IU CMCase ml^–1, 45 IU Avicelase ml^–1, and 137 IU -glucosidase ml^–1 with productivity of 326 IU l^–1 h^–1, which were 10--32% higher than the values obtained in shake-flask culturesRevisions requested 12 October 2004/1 November 2004; Received received 1 November 2004/14 December 2004     

Efficient secretion of human lysozyme from the yeast, <Emphasis Type="Italic">Kluyveromyces lactis</Emphasis>

Efficient secretion of human lysozyme from the yeast, Kluyveromyces lactis, was achieved by using more stable vectors in the order of S11 replication origin-containing episomal vector < full-length K. lactis plasmid pKD1-containing vector < centromeric vector < chromosome-integrated vectors. Cells containing a PGK (phosphoglycerate kinase) promoter-driven integration vector grown in non-selective rich medium achieved the highest level of secretion, 100 g lysozyme secretion ml ^–1 culture: this level was 10-fold higher than that achieved by episomal vectors. An additional copy of the protein disulfide isomerase gene further facilitated the secretion.     

Influence of growth conditions on the nisin production of bioengineered <Emphasis Type="Italic">Lactococcus lactis</Emphasis> strains

Nisin production of three bioengineered strains, (LAC338, LAC339 and LAC340) with immunity (nisFEG) and/or regulation (nisRK) genes of nisin biosynthesis on plasmids in the Lactococcus lactis LL27 nisin producer, was evaluated under pH-controlled and pH-uncontrolled batch fermentations. Optimization studies showed that fructose and yeast extract yielded the highest nisin activity. The strains LAC338, LAC339, and LAC340 produced 24, 45, and 44% more nisin, respectively, than wild-type L. lactis LL27 after 12-h incubation. However, sharp decreases in the yield of nisin were observed at the late phase of fermentation with LAC339 and LL27 in contrast to LAC340 and LAC338 strains for which the high level of nisin could be maintained longer. Obviously, increasing the copy number of the regulation genes together with immunity genes in the nisin producers retarded the loss of nisin in the late phase of the fermentation.     

Production of nisin Z using <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1 from hydrolyzed sago starch

A membrane bioreactor for production of nisin Z was constructed using Lactococcus lactis IO-1 in continuous culture using hydrolyzed sago starch as carbon source. A strategy used to enhance the productivity of nisin Z was to maintain the cells in a continuous growth at high cell concentration. This resulted in a volumetric productivity of nisin Z, as 50,000 IU l⁻¹ h⁻¹ using a cell concentration of 15 g l⁻¹, 30^°C, pH 5.5 and a dilution rate of 1.24 h⁻¹. Adding 10 g l⁻¹ YE and 2 g l⁻¹ polypeptone, other inducers were unnecessary to maintain production of nisin. The operating conditions of the reactor removed nisin and lactate, thus minimizing their effects which allowed the maintenance of cells in continuous exponential growth phase mode with high metabolic activity.     

Cycle changing the medium results in increased nisin productivity per cell in <Emphasis Type="Italic">Lactococcus lactis</Emphasis>

High specific cellular nisin production was aimed by cycle changing the medium of Lactococcus lactis N8 and LAC48. The highest level of nisin production was reached with the 120 min cycles but maximal production was unstable. In shorter cycles (30 and 60 min) cells could be maintained in a high production state up to the end of the fermentation (28 and 14 cycles). N8 produced 19-fold and LAC48 15-fold more nisin with cycle changing the medium than without cycle incubation.     

The <Emphasis Type="Italic">Lactococcus lactis</Emphasis> FabF fatty acid synthetic enzyme can functionally replace both the FabB and FabF proteins of <Emphasis Type="Italic">Escherichia coli</Emphasis> and the FabH protein of <Emphasis Type="Italic">Lactococcus lactis</Emphasis>

The genome of Lactococcus lactis encodes a single long chain 3-ketoacyl-acyl carrier protein synthase. This is in contrast to its close relative, Enterococcus faecalis, and to Escherichia coli, both of which have two such enzymes. In E. faecalis and E. coli, one of the two long chain synthases (FabO and FabB, respectively) has a role in unsaturated fatty acid synthesis that cannot be satisfied by FabF, the other long chain synthase. Since L. lactis has only a single long chain 3-ketoacyl-acyl carrier protein synthase (annotated as FabF), it seemed likely that this enzyme must function both in unsaturated fatty acid synthesis and in elongation of short chain acyl carrier protein substrates to the C18 fatty acids found in the cellular phospholipids. We report that this is the case. Expression of L. lactis FabF can functionally replace both FabB and FabF in E. coli, although it does not restore thermal regulation of phospholipid fatty acid composition to E. coli fabF mutant strains. The lack of thermal regulation was predictable because wild-type L. lactis was found not to show any significant change in fatty acid composition with growth temperature. We also report that overproduction of L. lactis FabF allows growth of an L. lactis mutant strain that lacks the FabH short chain 3-ketoacyl-acyl carrier protein synthase. The strain tested was a derivative (called the ∆fabH bypass strain) of the original fabH deletion strain that had acquired the ability to grow when supplemented with octanoate. Upon introduction of a FabF overexpression plasmid into this strain, growth proceeded normally in the absence of fatty acid supplementation. Moreover, this strain had a normal rate of fatty acid synthesis and a normal fatty acid composition. Both the ∆fabH bypass strain that overproduced FabF and the wild type strain incorporated much less exogenous octanoate into long chain phospholipid fatty acids than did the ∆fabH bypass strain. Incorporation of octanoate and decanoate labeled with deuterium showed that these acids were incorporated intact as the distal methyl and methylene groups of the long chain fatty acids.     

Enhancement of Nisin Production by <Emphasis Type="Italic">Lactococcus lactis</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis>

Lactococcus lactis subsp lactis BSA (L. lactis BSA) was isolated from a commercial fermented product (BSA Food Ingredients, Montreal, Canada) containing mixed bacteria that are used as starter for food fermentation. In order to increase the bacteriocin production by L. lactis BSA, different fermentation conditions were conducted. They included different volumetric combinations of two culture media (the Man, Rogosa and Sharpe (MRS) broth and skim milk), agitation level (0 and 100 rpm) and concentration of commercial nisin (0, 0.15, and 0.30 µg/ml) added into culture media as stimulant agent for nisin production. During fermentation, samples were collected and used for antibacterial evaluation against Lactobacillus sakei using agar diffusion assay. Results showed that medium containing 50 % MRS broth and 50 % skim milk gave better antibacterial activity as compared to other medium formulations. Agitation (100 rpm) did not improve nisin production by L. lactis BSA. Adding 0.15 µg/ml of nisin into the medium-containing 50 % MRS broth and 50 % skim milk caused the highest nisin activity of 18,820 AU/ml as compared to other medium formulations. This activity was 4 and ~3 times higher than medium containing 100 % MRS broth without added nisin (~4700 AU/ml) and 100 % MRS broth with 0.15 µg/ml of added nisin (~6650 AU/ml), respectively.     

Hyaluronic acid production by recombinant <Emphasis Type="Italic">Lactococcus lactis</Emphasis>

A gene encoding a new xylanase, named xynZG, was cloned by the genome-walking PCR method from the nematophagous fungus Plectosphaerella cucumerina. The genomic DNA sequence of xynZG contains a 780 bp open reading frame separated by two introns with the sizes of 50 and 46 bp. To our knowledge, this would be the first functional gene cloned from P. cucumerina. The 684 bp cDNA was cloned into vector pHBM905B and transformed into Pichia pastoris GS115 to select xylanase-secreting transformants on RBB-xylan containing plate. The optimal secreting time was 3 days at 25°C and enzymatic activities in the culture supernatants reached the maximum level of 362 U ml⁻¹. The molecular mass of the enzyme was estimated to be 19 kDa on SDS-PAGE. The optimal pH and temperature of the purified enzyme is 6 and 40°C, respectively. The purified enzyme is stable at room temperature for at least 10 h. The K _m and V _max values for birchwood xylan are 2.06 mg ml⁻¹ and 0.49 mmol min⁻¹mg⁻¹, respectively. The inhibitory effects of various mental ions were investigated. It is interesting to note that Cu²⁺ ion, which strongly inhibits most other xylanases studied, reduces enzyme activity by only 40%. Furthermore, enzyme activity is unaffected by EDTA even at a concentration of 5 mM.     

Identification and Characteristics of Nisin Z-Producing <Emphasis Type="Italic">Lactococcus lactis</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> Isolated from Kimchi

We isolated bacteriocin-producing Lactococcus lactis subsp. lactis from Kimchi. The bacteriocin inhibited strains of Clostridium perfringens, C. difficile, Listeria monocytogenes, vancomycin-resistant Enterococcus, and one out of four methicillin-resistant Staphylococcus aureus strains, as well as some closely related lactic acid bacteria. In tricine-SDS-PAGE, the bacteriocin migrated with an apparent molecular weight of about 4 kDa to the same location as nisin A and crude nisin Z. The gene encoding this bacteriocin was found to be identical to that of nisin Z with direct PCR sequence methods. The inhibitory activity was stable against heat and pH, but it was lost at 100°C for 1 h and at 121°C for 15 min. The bacteriocin was inactivated by proteolytic enzymes, but was not affected by lysozyme, lipase, catalase, or β-glucosidase. There were some differences in characteristics from those of nisins described previously. Received: 21 June 2002 / Accepted: 22 July 2002     

Enhanced expression of heterologous inulinase in <Emphasis Type="Italic">Kluyveromyces lactis</Emphasis> by disruption of <Emphasis Type="Italic">hap1</Emphasis> gene

Inulinase gene (Kcinu) derived from Kluyveromyces cicerisporus was expressed extracellularly in Kluyveromyces lactis using an episomal vector directed by Kcinu promoter. The influence of hap1 gene disruption on the expression of inulinase was studied. Inulinase activity in the supernatant of the recombinant Klhap1Δ strain was 391 U ml⁻¹ after cultured 120 h, which was 2.2-fold that of the wild type host. The relative inulinase mRNA level of the Klhap1Δ strain was 11.3-fold that of the wild type strain, and the expression plasmid was more stable in the mutant host. Based on these results, the disruption of hap1 facilitated the high and stable expression of inulinase controlled by Kcinu promoter in K. lactis.     

Optimization of culture conditions for the production of an extracellular ribonuclease by <Emphasis Type="Italic">Aspergillus niger</Emphasis> in a benchtop bioreactor

SummarySelf-directing optimization was successfully employed to determine the optimal combination of engineering parameters, viz., pH, aeration rate and agitation rate, for extracellular ribonuclease production by Aspergillus niger SA-13-20 in a batch bioreactor. Maximal RNase production of 5.38 IU ml^–1 was obtained at controlled pH of 2.33, aeration rate of 1.67 v/v/m and agitation rate of 850 rev/min. The effect of oxygen on the fermentation was also investigated. With increase in volumetric oxygen transfer coefficients (K_La), cell growth and RNase production first increased and then decreased. RNase production was further increased to 7.10 IU ml^–1 and the fermentation time was shortened from 96 to 72 h by controlling dissolved oxygen concentration at 10% saturation by aerating oxygen after about 28 h of fermentation under the above optimal condition. The kinetic model showed that RNase production by A. niger SA-13-20 was growth-associated.     

Anaerobic and aerobic continuous cultures of<Emphasis Type="Italic"> Saccharomyces cerevisiae</Emphasis>: comparison of plasmid stability and<Emphasis Type="Italic"> EXG1</Emphasis> gene expression

Two bioreactor continuous cultures, at anaerobic and aerobic conditions, were carried out using a recombinant Saccharomyces cerevisiae strain that over-expresses the homologous gene EXG1. This recombinant system was used to study the effect of dissolved oxygen concentration on plasmid stability and gene over-expression. Bioreactor cultures were operated at two dilution rates (0.14 and 0.03 h^–1) to investigate the effect of other process parameters on EXG1 expression. Both cultures suffered severe plasmid instability during the first 16 generations. Segregational plasmid loss rate for the aerobic culture was two-fold that of the anaerobic operation. In spite of this fact, exo--glucanase activity at aerobic conditions was 12-fold that of the anaerobic culture. This maximal activity (30 U ml^–1) was attained at the lowest dilution rate when biomass reached its greatest value and glucose concentration was zero.     

A repeated batch process for cultivation of <Emphasis Type="Italic">Bifidobacterium longum</Emphasis>

A repeated batch process was performed to culture Bifidobacterium longum CCRC 14634. An on-line device, oxidation-reduction potential (ORP), was used to monitor cell growth and uptake of nutrients in the culture. The ORP of the culture medium decreased substantially during fermentation until nutrients were depleted. Six cycles of batch fermentation using ORP as a control parameter were successfully carried out. As soon as ORP remained constant or increased, three-quarters of the broth was removed, and the same volume of fresh medium was fed to the fermenter for a new cycle of cultivation. Average cell concentrations of 1.9×10⁹ and 3.4×10⁹ cfu ml^–1 for repeated batch fermentation in MRS (Lactobacilli MRS broth) and WY (containing whey hydrolyzates, yeast extract, l-cysteine) medium, respectively, were achieved. Cell mass productivities for batch, fed-batch and repeated batch fermentation using MRS medium were 0.51, 0.41, and 0.64 g l^–1 h^–1, respectively, and those for batch and repeated batch using WY medium were 0.76, 0.99 g l^–1 h^–1, respectively. The results indicate a possible industrial process to culture Bifidobacteria sp.     

Quantification of the contribution of surface outgrowth to biocatalysis in sol-gels: oxytetracycline production by <Emphasis Type="Italic">Streptomyces rimosus</Emphasis>

A technique was developed for differentiating the activity of microbes solely within sol gels by using the contribution of biomass outgrowth. Streptomyces rimosus was immobilised in colloidal silica gels and biomass growth, oxytetracycline synthesis, pH and carbohydrate consumption were compared for UV surface-sterilised gels, untreated gels, and liquid cultures. Absolute and biomass specific oxytetracycline yields were higher for non-sterile gels than for liquid culture. Biomass solely within colloidal silica gels (1.7 mg ml^–1), and gels obtained from colloidal silica modified by addition of larger silica particles (1.2 mg ml^–1) yielded 27 and 21 g ml^–1 oxytetracycline compared with 97 and 104 g ml^–1 for unsterilised gels (3.6 and 5.2 mg ml^–1 biomass) displaying outgrowth. It was therefore apparent that biomass and antibiotic production within the gels was limited and that optimisation requires gel modification.     

Micro-encapsulation of <Emphasis Type="Italic"> Bifidobacterium lactis</Emphasis> for incorporation into soft foods

Summary Micro-encapsulation of the probiotic micro-organism Bifidobacterium lactis isolated from a bio-yoghurt starter culture, was carried out using a mixture of hydrated gellan and xanthan gums. Rheological studies showed that the gum mix was suitable for encapsulation of B. lactis, for incorporation into soft foods/beverages. The gel behaved as a non-Newtonian material, and the flow curve fitted well to the Herschel–Bulkley model. The average yield stress of the gum was 1.515 Pa, indicating gum stability, and the yield stress range was 1 Pa over a temperature range of 35–50 °C. Almost constant minimum gum viscosity occurred between 46 and 61 °C. Oval/round capsules were synthesized manually using a monoaxial gum flow through a 27.5 G bevelled needle, together with a superposed air stream (air knife technique). The diameter of the capsules, measured using laser diffractometry, varied from 20 to 2200μm, with 50% of the capsules having a diameter of ≤637 μm. Numbers of viable B. lactis in the capsules were estimated using high power ultrasound (20 kHz). By using a concentrated inoculum of B. lactis, microcapsules containing log₁₀ 11–12 c.f.u. g−1 were synthesized. Apart from the anaerobic culturing of B. lactis, all other work was done in the presence of atmospheric oxygen. The organism exhibited a high degree of oxygen tolerance. A 21-day survival study of immobilized cells in 1 M sodium phosphate buffer (pH 7) stored at either 4 or 22 °C indicated that B. lactis survived in excess of log₁₀ 11 c.f.u. g−1 microcapsule. This technique represents a suitable means of supplying viable probiotics to the food and/or pharmaceutical industries.     

Characteristics of the bacteriocin produced by <Emphasis Type="Italic">Lactococcus lactis</Emphasis> subsp. <Emphasis Type="Italic">cremoris</Emphasis> CTC 204 and the effect of this compound on the mesophilic bacteria associated with raw beef

Summary >Screening for the bacteriocin production of strains of lactic acid bacteria from various meat and meat products resulted in the detection of a bacteriocin-producing Lactococcus lactis subsp. cremoris CTC 204, isolated from chicken. The bacteriocin inhibited not only closely related lactic acid bacteria (Lactobacillus helveticus), but also pathogenic microorganisms (Staphylococcus aureus, Listeria monocytogenes, Bacillus cereus, and Clostridium perfringens). It was inactivated by α-chymotrypsin, ficin, papain, and pronase E, but not by lipase or pepsin. This compound was heat stable even at autoclaving temperature (121°C for 10min) and was produced during refrigerated storage. It was also active over a wide pH range (2–10), but the highest activity was observed in the lower pH range. The results indicated that dipping raw beef in the bacteriocin produced by strain CTC 204 could contribute to the extension of the shelf life of refrigerated bovine meat.     

Optimization of lactic acid production by immobilized <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1

Production of lactic acid from glucose by immobilized cells of Lactococcus lactis IO-1 was investigated using cells that had been immobilized by either entrapment in beads of alginate or encapsulation in microcapsules of alginate membrane. The fermentation process was optimized in shake flasks using the Taguchi method and then further assessed in a production bioreactor. The bioreactor consisted of a packed bed of immobilized cells and its operation involved recycling of the broth through the bed. Both batch and continuous modes of operation of the reactor were investigated. Microencapsulation proved to be the better method of immobilization. For microencapsulated cells at immobilized cell concentration of 5.3 g l⁻¹, the optimal production medium had the following initial concentrations of nutrients (g l⁻¹): glucose 45, yeast extract 10, beef extract 10, peptone 7.5 and calcium chloride 10 at an initial pH of 6.85. Under these conditions, at 37 °C, the volumetric productivity of lactic acid in shake flasks was 1.8 g l⁻¹ h⁻¹. Use of a packed bed of encapsulated cells with recycle of the broth through the bed, increased the volumetric productivity to 4.5 g l⁻¹ h⁻¹. The packed bed could be used in repeated batch runs to produce lactic acid.     

Conjugative plasmid pIP501 undergoes specific deletions after transfer from<Emphasis Type="Italic"> Lactococcus lactis</Emphasis> to<Emphasis Type="Italic"> Oenococcus oeni</Emphasis>

Conjugal transfer of plasmids pIP501 and its derivative pVA797 from Lactococcus lactis to Oenococcus oeni was assayed by filter mating. Plasmid pIP501 was transferred to a number of O. oeni strains whereas a single transconjugant of O. oeni M42 was recovered when pVA797 was used. Physical analysis of the transconjugant plasmids revealed that pIP501 and pVA797 underwent extensive deletions in O. oeni that affected the tra region (conjugal transfer) and SegB region (stability). All derivatives showed segregational instability in O. oeni, but were stably maintained in L. lactis. These differences correlated with the different plasmid copy numbers and the extent of deletions within the SegB region.Abbreviations CAT Chloramphenicol acetyltransferase - MLS Macrolides-lincosamides-streptogramin B resistance