Effects of pH profiles on nisin fermentation coupling with foam separation

Online foam separation was proposed to recover nisin during fermentation of Lactococcus lactis subsp. lactis ATCC 11454. Firstly, the optimal pH profile of nisin fermentation was investigated including different realkalization set values and pH drop gradients. Then the selected pH profiles of 5.75 ± 0.05 and 6.25–5.75 (±0.02) were used to perform nisin fermentation coupling with foam separation. The results showed that pH profile of 5.75 ± 0.05 was better than that of 6.25–5.75 (±0.02) for online foam separation. With the optimal pH profile, an aeration of 20 ml min⁻¹ that started at 8 h of incubation and lasted for 2 h resulted in 6.6 times higher specific productivity than that of the fermentation without aeration. Nisin synthesis was therefore prolonged with low sucrose concentration in the culture broth, which indicated that the feedback inhibition of nisin is more influential than the substrate limitation of sucrose in the late phase of nisin fermentation. Total nisin production (4,870 ± 180 IU ml⁻¹) was increased by 30.3% with online foam separation. This effective online recovery method for nisin production could be easily scaled up due to the facile operation of foaming process.     

Effects of pH profiles on nisin production in biofilm reactor

Apart from its widely accepted commercial applications as a food preservative, nisin emerges as a promising alternative in medical applications for bacterial infection in both humans and livestock. Improving nisin production through optimization of fermentation parameters would make nisin more cost-effective for various applications. Since nisin production by Lactococcus lactis NIZO 22186 was highly influenced by the pH profile employed during fermentation, three different pH profiles were evaluated in this study: (1) a constant pH profile at 6.8 (profile 1), (2) a constant pH profile with autoacidification at 4 h (profile 2), and (3) a stepwise pH profile with pH adjustment every 2 h (profile 3). The results demonstrated that the low-pH stress exerted during the first 4 h of fermentation in profile 3 detrimentally affected nisin production, resulting in a very low maximum nisin concentration (593 IU ml⁻¹). On the other hand, growth and lactic acid production were only slightly delayed, indicating that the loss in nisin production was not a result of lower growth or shifting of metabolic activity toward lactic acid production. Profile 2, in which pH was allowed to drop freely via autoacidification after 4 h of fermentation, was found to yield almost 1.9 times higher nisin (3,553 IU ml⁻¹) than profile 1 (1,898 IU ml⁻¹), possibly as a result of less adsorption of nisin onto producer cells. Therefore, a combination of constant pH and autoacidification period (profile 2) was recommended as the pH profile during nisin production in a biofilm reactor.     

Promoting acid resistance and nisin yield of <Emphasis Type="Italic">Lactococcus lactis</Emphasis> F44 by genetically increasing D-Asp amidation level inside cell wall

Nisin fermentation by Lactococcus lactis requires a low pH to maintain a relatively higher nisin activity. However, the acidic environment will result in cell arrest, and eventually decrease the relative nisin production. Hence, constructing an acid-resistant L. lactis is crucial for nisin harvest in acidic nisin fermentation. In this paper, the first discovery of the relationship between D-Asp amidation-associated gene (asnH) and acid resistance was reported. Overexpression of asnH in L. lactis F44 (F44A) resulted in a sevenfold increase in survival capacity during acid shift (pH 3) and enhanced nisin desorption capacity compared to F44 (wild type), which subsequently contributed to higher nisin production, reaching 5346 IU/mL, 57.0% more than that of F44 in the fed-batch fermentation. Furthermore, the engineered F44A showed a moderate increase in D-Asp amidation level (from 82 to 92%) compared to F44. The concomitant decrease of the negative charge inside the cell wall was detected by a newly developed method based on the nisin adsorption amount onto cell surface. Meanwhile, peptidoglycan cross-linkage increased from 36.8% (F44) to 41.9% (F44A), and intracellular pH can be better maintained by blocking extracellular H⁺ due to the maintenance of peptidoglycan integrity, which probably resulted from the action of inhibiting hydrolases activity. The inference was further supported by the acmC-overexpression strain F44C, which was characterized by uncontrolled peptidoglycan hydrolase activity. Our results provided a novel strategy for enhancing nisin yield through cell wall remodeling, which contributed to both continuous nisin synthesis and less nisin adsorption in acidic fermentation (dual enhancement).     

Effects of fed-batch fermentation and pH profiles on nisin production in suspended-cell and biofilm reactors

A biofilm reactor not only shortens the lag phase of nisin production, but also enhances nisin production when combined with an appropriate pH profile. Due to the substrate inhibition that takes place at high levels of carbon source, fed-batch fermentation was proposed as a better alternative for nisin production. In this study, the combined effects of fed-batch fermentation and various pH profiles on nisin production in a biofilm reactor were evaluated. The tested pH profiles include 1) a constant pH profile at 6.8 (profile 1), 2) a constant pH profile with an autoacidification after 4 h (profile 2), and 3) a step-wise pH profile with pH adjustment every 2 h (profile 3). When profile 1 was applied, fed-batch fermentation enhanced nisin production for both suspended-cell (4,188 IU ml⁻¹) and biofilm (4,314 IU ml⁻¹) reactors, yielded 1.8- and 2.3-fold higher nisin titer than their respective batch fermentation. On the other hand, pH profiles that include periods of autoacidification (profiles 2 and 3) resulted in a significantly lower nisin production in fed-batch fermentation (2,494 and 1,861 IU ml⁻¹ for biofilm reactor using profile 2 and 3, respectively) due to toxicity of excess lactic acid produced during the fermentation. Overall, this study suggested that fed-batch fermentation can be successfully used to enhance nisin production for both suspended-cell and biofilm reactors.     

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.     

Lantibiotic nisin Z fermentative production by Lactococcus lactis IO-1: relationship between production of the lantibiotic and lactate and cell growth

 The influence of several parameters on the fermentative production of nisin Z by Lactococcus lactis IO-1 was studied. Considerable attention has been focused on the relationship between the primary metabolite production of bacteriocin and lactate and cell growth, which has so far not been clarified in detail. Production of nisin Z was optimal at 30°C and in the pH range 5.0–5.5. The addition of Ca²⁺ to the medium showed a stimulating effect on the production of nisin Z. A maximum activity of 3150 IU/ml was obtained during pH-controlled batch fermentation in the medium supplemented with 0.1 M CaCl₂. It was about three times higher than that obtained under the optimal conditions for cell growth and lactic acid production. Received: 12 July 1995/Received revision: 11 September 1995/Accepted: 4 October 1995     

Improving nisin production by increasing nisin immunity/resistance genes in the producer organism Lactococcus lactis

The effect on nisin production of increasing nisin immunity/resistance genes in Lactococcus lactis subsp. lactis MG1363 was investigated. The 60-kb nisin immunity/resistance plasmid pND300, which was isolated from a non-nisin-producing strain, encodes five genes involved in nisin immunity/resistance, which are very similar to those of the immunity/resistance system encoded by the nisin-production transposon. The introduction of pND300 into MG1363(TnNip) resulted in the construct being able to produce significantly more nisin than the parent MG1363(TnNip). The introduction of pND314, which contains the nisin immunity/resistance genes subcloned into pSA3, into MG1363(TnNip) allowed the strain to grow more rapidly than the parent MG1363(TnNip) with a concomitant increase in the rate of nisin production. This work illustrates that introduction of pND300 and a derivative containing the nisin immunity/resistance system of pND300 into MG1363 (TnNip) can result in significant alterations to the kinetics of nisin production. These observations indicate approaches that may be used successfully to improve the economics of nisin production. Received: 11 February 1998 / Received revision: 25 June 1998 / Accepted: 27 June 1998     

Nisin高产菌株的高通量筛选

【目的】乳酸链球菌素(nisin)是一种天然生物活性抗菌肽,对包括食品腐败菌和致病菌在内的许多革兰氏阳性菌具有强烈的抑制作用,而用作食品的防腐剂。本研究通过建立高通量筛选方法,实现高效快速省力的高产菌株筛选,为工业上筛选高产菌株提供研究方案。【方法】通过对Lactococcus lactis ATCC11454菌株进行紫外诱变,获得2511株突变株。利用Biomek FXP自动工作站建立96微孔板的高通量筛选方法,突变株经高通量挑选、菌种培养及菌液稀释后,加入到生长至对数中期的藤黄微球菌中,采用改进后的比浊法快速检测nisin生物活性。用此方法对突变株进行初筛、复筛后可得到nisin高产菌株,并通过摇瓶发酵评估高通量筛选方法。【结果】确定比浊法检测的条件为:nisin活性稀释在10–25 IU/m L范围内,与藤黄微球菌反应2 h后检测藤黄微球菌的菌体量(OD600)。2511株突变株经过2轮高通量筛选,最终获得约50株产量提升的菌株,对其中8株进行摇瓶精确测量,显示产量均有提高,并且其中一株产量提升了30%,成功建立了高通量筛选nisin高产菌株的方法。【结论】利用比浊检测法,在其基础上成功建立高通量筛选高产nisin菌的方法,经过初筛复筛,整个周期由1人耗时5 d即可完成2511株突变株的筛选工作。相较于传统的选育方法,高通量筛选具有快速、稳定、高效的特点,提高了筛选效率,缩短了选育周期,是工业上筛选高产nisin菌的有效手段。     

Development of a low-cost medium for production of nisin from Lactococcus lactis subsp. lactis

The goal of this project was to develop a lower-cost medium for nisin production, so this bacteriocin could be used in a broader range of industrial fermentation processes. The objectives included: (1) evaluating methods for controlling the inhibitory effect of lactic acid produced during fermentation, and (2) comparing two inexpensive complex media for nisin production. Lactococcus lactis subsp. lactis was cultured in shake flasks on Laurel–Tryptose broth to evaluate a range of buffers for pH control. NaHCO₃ proved to be an effective buffer for increasing nisin production. Subsequent trials then evaluated condensed corn soluble (CCS, a fuel ethanol production byproduct) and cheese whey as inexpensive growth media. CCS was shown to be an efficient, low-cost medium for high nisin titers and yields. These modifications reduced the medium costs for nisin production from $600/kg nisin (based on Laurel–Tryptose broth medium) to $35–40/kg nisin for the corn solubles medium.     

The role of nisin in fuel ethanol production with Saccharomyces cerevisiae

Aims: To investigate the effects of nisin on lactobacilli contamination of yeast during ethanol fermentation and to determine the appropriate concentration required to control the growth of selected lactobacilli in a YP/glucose media fermentation model. Methods and Results: The lowest concentration of nisin tested (5 IU ml^?1) effectively controlled the contamination of YP/glucose media with 10⁶ CFU ml^?1 lactobacilli. Lactic acid yield decreased from 5·0 to 2·0 g l^?1 and potential ethanol yield losses owing to the growth and metabolism of Lactobacillus plantarum and Lactobacillus brevis were reduced by 11 and 7·8%, respectively. Approximately, equal concentrations of lactic acid were produced by Lact. plantarum and Lact. brevis in the presence of 5 and 2 IU ml^?1 nisin, respectively, thus demonstrating the relatively higher nisin sensitivity of Lact. brevis for the strains in this study. No differences were observed in the final ethanol concentrations produced by yeast in the absence of bacteria at any of the nisin concentrations tested. Conclusions: Metabolism of contaminating bacteria was reduced in the presence of 5 IU ml^?1 nisin, resulting in reduced lactic acid production and increased ethanol production by the yeast. Significance and Impact of the Study: Bacteriocins represent an alternative to the use of antibiotics for the control of bacterial contamination in fuel ethanol plants and may be important in preventing the emergence of antibiotic‐resistant contaminating strains.     

Modelling the production of nisin by Lactococcus lactis in fed-batch culture

Nisin production in batch culture and fed-batch cultures (sucrose feeding rates were 6, 7, 8, and 10 g l^–1 h^–1, respectively) by Lactococcus lactis subsp. lactis ATCC 11454 was investigated. Nisin production showed primary metabolite kinetics, and could be improved apparently by altering the feeding strategy. The nisin titer reached its maximum, 4,185 IU ml^–1, by constant addition of sucrose at a feeding rate of 7 g l^–1 h^–1; an increase in 58% over that of the batch culture (2,658 IU ml^–1). Nisin biosynthesis was affected strongly by the residual sucrose concentration during the feeding. Finally, a mathematical model was developed to simulate the cell growth, sucrose consumption, lactic acid production and nisin production. The model was able to describe the fermentation process in all cases.     

Improvement of nisin production in pH feed-back controlled,fed-batch culture by <Emphasis Type="Italic">Lactococcus lactis</Emphasis>subsp<Emphasis Type="Italic">. lactis</Emphasis>

Nisin production by Lactococcus lactis subsp. lactisin fed-batch culture was doubled by using a pH feed-back controlled method. Sucrose concentration was controlled at 10 g l^–1 giving 5010 IU nisin ml^–1 compared to 2660 IU nisin ml^–1 in batch culture.     

The effect of nisin on Listeria monocytogenes in culture medium and long-life cottage cheese

M.A.S.S. FERREIRA AND B.M. LUND. 1996. The sensitivity to nisin of 27 strains of Listeria monocytogenes , four of L. innocua and one of L. ivanovii was estimated at pH 6.8 and pH 5.5. Strains of L. monocytogenes showed differences in sensitivity which were not correlated with serotype. Strains of L. innocua were as resistant as the most resistant strains of L. monocytogenes , whereas the strain of L. ivanovii was relatively sensitive. Two of the most resistant strains of L. monocytogenes multiplied in aerated liquid medium adjusted to pH 5.0 with HCl, incubated at 20°C; nisin, 500 IU ml^-1, prevented multiplication and caused death. Following inoculation of a resistant strain into long-life cottage cheese, pH 4.6–4.7, the number of viable L. monocytogenes decreased approximately 10-fold during storage at 20°C for 7 d; addition of nisin, 2000 IU g^-1, to the cottage cheese increased the rate of inactivation to approximately a 1000-fold decrease in 3 d.     

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.     

Lactate removal by anionic-exchange resin improves nisin production by Lactococcus lactis

When lactate was removed from sucrose fermentation in situ, using the anionic-exchange resin Amberlite IRA-67, by Lactococcus lactis growing in batch culture, nisin production increased by two-fold when compared to the alkali pH-controlled fermentation. In comparison to sucrose, lactate removal increased nisin production 1.5-fold and 0.3-fold when galactose and glucose were used as carbon sources respectively.     

Immobilization of nisin producer Lactococcus lactis strains to chitin with surface-displayed chitin-binding domain

In this study, nisin producer Lactococcus lactis strains displaying cell surface chitin-binding domain (ChBD) and capable of immobilizing to chitin flakes were constructed. To obtain ChBD-based cell immobilization, Usp45 signal sequence with ChBD of chitinase A1 enzyme from Bacillus circulans was fused with different lengths of PrtP (153, 344, and 800 aa) or AcmA (242 aa) anchors derived from L. lactis. According to the whole cell ELISA analysis, ChBD was successfully expressed on the surface of L. lactis cells. Scanning electron microscope observations supported the conclusion of the binding analysis that L. lactis cells expressing the ChBD with long PrtP anchor (800 aa) did bind to chitin surfaces more efficiently than cells with the other ChBD anchors. The attained binding affinity of nisin producers for chitin flakes retained them in the fermentation during medium changes and enabled storage for sequential productions. Initial nisin production was stably maintained with many cycles. These results demonstrate that an efficient immobilization of L. lactis cells to chitin is possible for industrial scale repeated cycle or continuous nisin fermentation.     

The effect of nisin concentration and nutrient depletion on nisin production of Lactococcuslactis

The kinetics of nisin production was studied in batch cultures using a construct of Lactococcuslactis subsp. lactis C2SmPrt⁻, containing a transposon (TnNip) that encodes nisin production. The introduction of TnNip into C2SmPrt⁻significantly lowered the specific growth rate and the maximum A ₆₂₀ reached was reduced from 15.2 to 11.0. The effect of nisin concentration and nutrient depletion on nisin production of the construct, C2SmPrt⁻(TnNip), was examined. Nisin production was found to be inhibited by high concentrations of nisin, when grown in excess nutrient, even though growth of the culture continued because nutrient limitation was not operating. However, in low nutrient concentrations nisin production was limited by nutrient depletion. The specific growth rate of C2SmPrt⁻(TnNip) was altered, by using different nutrient concentrations and different sugars, in order to examine the relationship between nisin production and growth. Nisin production was shown to be growth-associated for most of growth, but near the end of growth, when the specific growth rate was 0.05 h⁻¹ or less, the production ceased. Received: 20 March 1997 / Received revision: 10 June 1997 / Accepted: 14 June 1997     

Enhanced inactivation of Listeria monocytogenes by nisin in the presence of ethanol

AIMS: The effect of combinations of nisin and ethanol on the survival of Listeria monocytogenes was investigated. METHODS AND RESULTS: Killing by nisin was enhanced during simultaneous exposure to ethanol (2-7% v/v). For example, while 10 IU ml(-1) nisin reduced viability by 1 log unit in 20 min, a combination of this antimicrobial peptide and 5% ethanol, reduced numbers of surviving cells by 3 log units. Increasing the concentrations of either ethanol (2-7%) or nisin (10-50 IU ml(-1)) led to increased cell death with synergy being demonstrated for all combinations tested and at a range of temperatures from 5 to 37 degrees C. CONCLUSIONS: Ethanol can act synergistically with nisin to reduce the survival of L. monocytogenes. SIGNIFICANCE AND IMPACT OF THE STUDY: Combinations of ethanol and nisin may be feasible as an effective way of controlling this pathogen in the food processing environment.     

Enhanced ethanol production through selective adsorption in bacterial fermentation

To alleviate the ethanol inhibition of Escherichia coli KO11 (ATCC 55124), during fermentation, online ethanol sequestration was achieved using F-600 activated carbon. Two separate schemes were tested, one involving direct addition of activated carbon to the fermentation flask for the purpose of in-situ adsorption and a second involving an externally located activated carbon packed bed. For the in-situ ethanol adsorption experiments, varying amounts of adsorbent were added to the medium at the start of the fermentation. The addition of the activated carbon in the fermentation broth resulted in increased glucose utilization and ethanol production for all flasks containing activated carbon. For the control flasks, approximately 75% of the available substrate was utilized before the fermentation was inhibited. The entire glucose supply of flasks containing activated carbon was depleted. Ethanol production was also increased from 28 g/L for the control containing no activated carbon to nearly 45 g/L (including the ethanol in the adsorbed phase) for the flasks containing activated carbon. The implementation of an externally located packed bed adsorber for the purpose of on-line ethanol removal was tested over a number of adsorption cycles to evaluate the performance of the adsorption bed and the ethanol productivity. Results indicate that maintaining ethanol fermentation medium concentrations below 20 ∼ 30 g/L extends and enhances ethanol productivity. After 3 cycles over a period of 180 h, an additional 80% ethanol was produced when compared to the control experiments, despite the suboptimal acidic pH of the medium.