- Open Access
Optimization of the Lactococcus lactis nisin-controlled gene expression system NICE for industrial applications
© Mierau et al; licensee BioMed Central Ltd. 2005
- Received: 18 April 2005
- Accepted: 30 May 2005
- Published: 30 May 2005
The nisin-controlled gene expression system NICE of Lactococcus lactis is one of the most widely used expression systems in Gram-positive bacteria. Despite its widespread use, no optimization of the culture conditions and nisin induction has been carried out to obtain maximum yields. As a model system induced production of lysostaphin, an antibacterial protein (mainly against Staphylococcus aureus) produced by S. simulans biovar. Staphylolyticus, was used. Three main areas need optimization for maximum yields: cell density, nisin-controlled induction and protein production, and parameters specific for the target-protein.
In a series of pH-controlled fermentations the following parameters were optimized: pH of the culture, use of NaOH or NH4OH as neutralizing agent, the addition of zinc and phosphate, the fermentation temperature, the time point of induction (cell density of the culture), the amount of nisin added for induction and the amount of three basic medium components, i.e. yeast extract, peptone and lactose. For each culture growth and lysostaphin production was followed. Lysostaphin production yields depended on all parameters that were varied. In the course of the optimization a three-fold increase in lysostaphin yield was achieved from 100 mg/l to 300 mg/l.
Protein production with the NICE gene expression system in L. lactis strongly depends on the medium composition, the fermentation parameters and the amount of nisin added for induction. Careful optimization of key parameters lead to a significant increase in the yield of the target protein.
- High Cell Density
- Lactococcus Lactis
Overview of various applications of the NICE system
Expression of homologous genes
ATPase system (8 gene operon)
Cluster of genes encoding folate biosynthesis
Expression of heterologous genes of Gram+ and Gram- bacteria
NADH oxidase of Streptococcus mutans
Fructose bisphosphatase of Escherichia coli
Green fluorescent protein of Aequoria victoria
Lysostaphin of Staphylococcus simulans biovar. Staphylolyticus
Lipase of Staphylococcus hyicus
Membrane proteins: prokaryotic and eukaryotic
Multidrug transporter of Lactococcus lactis
Xylidose transporter of Lactobacillus pentosus
ATP/ADP translocator of Rickettsia prowazekii
KDEL receptor of Homo sapiens
Mitochondrial carriers of Saccharomyces cerevisiae
Cloning of toxic genes
Lysis cassette of the virulent phage us3 of
Autolysin gene of Leuconostoc citreum
Antigen L7/12 of Brucella abortus
C subunit of tetanus toxin (TTFC) of Clostridium tetani
Non-structural protein 4 of bovine rotavirus
Interleukin 12 of Homo sapiens
Lysostaphin of Staphylococcus simulans biovar. Staphylolyticus
Escherichia coli is, at present, the dominant prokaryotic system for industrial gene expression. This is due to high yields, ease in genetic handling, long-term experience and extensive documentation with the US Food and Drug Administration and other regulatory bodies. However, there are also various disadvantages, such as the formation of endotoxins, the formation of inclusion bodies, the presence of two membranes, which hampers secretion, and the relatively complicated aerobic fermentation [10, 11]. L. lactis, on the other hand, has a number of properties that make this bacterium an interesting alternative candidate for large-scale gene expression: the bacterium is food grade (used in food production for thousands of years), it is used at very large scales, and plasmid selection mechanisms are available that are food grade and self-cloning (e.g. growth on lactose) . Furthermore, no endotoxins or inclusion bodies are formed and sophisticated genetic tools enable easy genetic handling [13, 14]. Finally, simple, non-aerated fermentation makes direct scale-up from 1-L scale to 1000-L scale possible [2, 14]. Recently, we have demonstrated in our laboratory that nisin controlled gene expression can be effectively used in 3000-L scale fermentations .
The NICE system has been used in a multitude of laboratory applications (Table 1), in which gene expression is often performed in acidifying cultures. The drawback of this culture type is its low final cell density due to medium acidification by lactic acid. pH-controlled fermentations, on the other hand, result in at least five-fold higher cell densities and thus higher biomass yields. However, no systematic optimization of the induction and expression of the NICE system under pH-regulated conditions has yet been performed. Three main areas need optimization for maximum yields: cell density of the culture, nisin-controlled induction and protein production, and parameters specific for the target-protein.
Lysostaphin is a 25 kD antibacterial protein produced by Staphylococcus simulans biovar. Staphylolyticus  and mainly used against multiple antibiotic resistant S. aureus [17, 18]. In this paper we demonstrate, with lysostaphin as a model, that careful optimization of key parameters of the induction and production process can lead to an at least three-fold increase of the fermentation yield from 100 mg/L to 300 mg/L lysostaphin.
At present, protocols for nisin-induced gene expression only exist for acidifying batch cultures (see e.g. [7, 19]) but not for pH-controlled batch cultures. Therefore, a protocol that was previously developed at our laboratory for large-scale lysostaphin production  was used as a starting point. The cultivation and induction conditions were as follows: pH controlled (using NaOH) growth at pH 6.5, growth temperature 30°C, inoculum 1%, induction at OD600 = 1 (= 0.3 g/L cell dry weight ) with 10 ng/mL nisin, and harvest after 6 h. The initial medium composition was: 5% lactose, 1.5 % soy peptone, 1% yeast extract, 1 mM MgSO4 and 0.1 mM MnSO4.
In a series of 58 1-L fermentations the following parameters were tested and optimized: pH, neutralization agent, addition of phosphate and zinc, fermentation temperature, the time point of induction, i.e. cell density, the concentration of peptone, yeast extract and lactose in the medium and the lysostaphin production time after induction.
pH and neutralizing agent
Addition of phosphate and zinc
After these initial experiments, it was decided to set the following basic fermentation conditions: pH at 7.0, to use NH4OH as neutralizing agent, to add both 0.01 g/L sodium phosphate (Na2HPO4 *2 H2O) and 100 μM ZnSO4. To establish a baseline for lysostaphin production and to analyze the effect of phosphate or zinc on lysostaphin production, an induction experiment was carried out. Induction of lysostaphin production was initiated at OD600 = 1.0 with 10 ng/mL nisin. Figure 3 shows the basic pattern of growth and induction. After the addition of nisin, product formation begins immediately, and occurs parallel to growth. When lysostaphin production was induced, growth of the culture slowed down considerably about 30 min after induction. This is accompanied by a steep drop of the viable counts on lactose M17 agar plates of 4 orders of magnitude. However, despite the growth retardation, lysostaphin production was linear for 8 h before it abruptly ended (Figure 3) .
Combination of cell density at induction and the amount of added nisin
Addition of extra nutrients
Summary of the optimization
The highest production of lysostaphin was observed under the following conditions: the pH is fixed at 7.0, the temperature is 30°C, the neutralizing agent is NH4OH, medium components are 7% lactose, 2.5% peptone, 2% yeast extract, 0.01% sodium phosphate (Na2PO4 *2 H2O), 100 μM ZnSO4, 1 mM MgSO4 and 0.1 mM MnSO4, cells are grown to an OD600 = 5 and induced with 40 ng/mL nisin. Lysostaphin production proceeded for 6 to 8 hours and then abruptly stopped. After that time there may be a small decrease of lysostaphin concentration over time. However, this depended on the medium composition and the fermentation conditions (Figures 4, 6 and 7).
The nisin-controlled gene expression system NICE is widely used for a multitude of different applications. However, induction of this gene expression system has never been optimized for either laboratory conditions or for industrial-scale applications. In the present publication we show that the yield of the production of a heterologous protein can be increased at least three-fold by careful optimization of the fermentation and induction conditions. A number of general observations have been made:
(I) in a pH controlled culture, the point at which the pH is fixed and the neutralizing agent influence the general growth and biomass yield of the culture. A neutral pH and a mild neutralizing agent such as NH4OH was beneficial for growth of lactococci.
(II) Nisin induction works over a broad range of temperatures, even at 20°C. However, there is a clear correlation between the temperature of the fermentation and the speed and yield of the induction. The lower the temperature, the slower was the response to nisin and the lower was the yield of the heterologous protein. For lysostaphin production, a temperature of 30°C was found to be the optimum. Figure 4 may give a hint that it is worthwhile to also consider production at a lower temperature. At 25°C maximum lysostaphin production was slower and somewhat lower than at 30°C; however it seemed to be more stable in the cells, as can be seen at the end of the culture.
(III) Addition of extra and specific nutrients may be needed. Lysostaphin is a zinc-containing enzyme. Production of large amounts of active enzyme may be limited by the amount of zinc that is present in the different medium components. Therefore, extra zinc was added.
More generally, phosphate is needed for DNA biosynthesis and the energy metabolism of the cell. There are certain amounts of phosphorus compounds in the yeast extract and in the peptone, but growth at higher cell densities and product formation may require more phosphorus. Initially, little difference was seen after addition of phosphate, however, in an induction experiment at higher cell densities, strongly reduced product formation was observed (150 mg/L lysostaphin without extra phosphate versus 220 mg/L with phosphate). Zinc is an example of specific components that need to be selected and optimized for each target protein individually.
(IV) There is a strong correlation between the medium composition, the cell density of the culture at the moment of induction and the amount of nisin that is added. Induction is a dynamic process and needs growing cells both for the induction to occur and for the subsequent protein production to proceed as fast and as long as possible. In Figure 5 we saw increases in lysostaphin production after both the cell density for induction and the amount of nisin were increased. However, when the induction occurs too late in the growth cycle (e.g. OD600 = 7) no further product increase can be observed, even when more nisin was added. Similarly, if too much nisin is added (see Figure 7) it will become detrimental for product formation. Under the present conditions the maximum yield was reached at an OD600 around 5 with about 40 ng/mL nisin. These parameters can directly be used for the increased production of any other heterologous protein and as a starting point for further optimization of the respective process.
(V) As can be seen in Figure 6, lysostaphin production was still limited by the supply of nutrients in the fermentation medium. Addition of higher amounts of peptone, yeast extract and sugar significantly increased the production of lysostaphin. These parameters need to be carefully optimized, since they make up the highest costs of the growth medium.
The present publication outlines the optimization of controlled expression of heterologous genes in L. lactis using the NICE system. Careful optimization of a number of key parameters leads to a considerable increase in the overall yield of the target protein. The current outline gives a framework for this optimization. However, since every protein is different, a number of steps need to be checked and fine-tuned individually.
After the present round of optimization, the model protein lysostaphin could be produced up to 300 mg/L. Since lysostaphin has a growth-inhibiting effect on the host cells, and maybe also on its own production, a higher production capacity of the L. lactis host can be inferred for target proteins that do not have functionally detrimental effects on the host cells. Application of the described optimization to other target proteins will show the actual potential and limits of L. lactis for the industrial production of heterologous proteins.
The nisin-controlled gene expression system NICE of Lactococcus lactis is one of the most widely used Gram-positive gene expression systems. To date, no systematic study has been undertaken to optimize the system for maximum yields, especially for industrial scale applications. The present study shows that by careful optimization of growth, induction and target protein-specific parameters, an at least three-fold increase of the yield can be achieved.
Bacterial strains and growth media
Lactococcus lactis subsp. cremoris NZ3900  carrying plasmid pNZ1710 (plasmid with gene for mature lysostaphin under control of the nisA promoter; ) was stored as frozen stock in M17 medium  containing 0.5% lactose as carbon source and plasmid selection agent. The basic fermentation medium contained 5% lactose (Lactochem, Borculo Domo Ingredients, Zwolle, The Netherlands), 1.0% yeast extract (Biospringer, Maisons-Alfort, France), 1.5% soy peptone (Merck, VWR International, Amsterdam, The Netherlands), 1 mM MgSO4 and 0.1 mM MnSO4. All components were dissolved in water and sterilized at 110°C for 20 min. Additional components such as Na2HPO4 and ZnSO4 were filter sterilized and added separately.
Nisin for induction was prepared as follows: 0.04% nisin powder (Sigma-Aldrich Chemie, Zwijndrecht, The Netherlands) was dissolved in 0.05% acetic acid and precipitated proteins were removed by centrifugation. Nisin was added for induction as indicated in the Results section.
The strain was taken from stock and sub-cultured twice before inoculation. 1-L Applicon fermenters were used coupled to an Applicon Biocontroller ADI 1030 (Applicon, Frederiksberg, Denmark) for pH and temperature control. The pH of the culture was controlled at the indicated values (see Results) with either 2.5 M NaOH or 2.5 M NH4OH. The cell density was measured in samples that were taken at regular intervals, by determining the absorbance at 600 nm with a path length of 1 cm [OD600]. For lysostaphin measurements, cells of appropriate samples were sedimented by centrifugation and stored at -20°C. After thawing, cell density was adjusted to OD600 = 10 (according to the initial cell density reading) and 1 ml of the cell suspension was mixed with 1 g glass beads (0.1 mm Zirconia/Silica beads from Biospec products, Bartlesville, OK., U.S.A.) in screw-cap Eppendorf tubes. Subsequently, cells were subjected to bead-beating in a FastPrep beadbeater (FP120, QBiogene, Irivne, CA, U.S.A.), adjustment 4, 4 × 30 s. After the beads were allowed to sediment, lysostaphin concentration was determined in the whole cell extract.
Lysostaphin was quantified using SDS-capillary zone electrophoresis (SDS-CZE). The SDS sample buffer was prepared by dissolving in ca. 80 mL of water 606 mg of tris(hydroxymethyl)aminomethane (Tris), 1.00 g of sodium dodecylsulphate (SDS) and 37 mg of EDTA. Hydrochloric acid (0.1 M, 14.7 mL) was added and the solution was made up to 100 mL. Daily, 25 mg of DTT was added to 10 mL SDS sample buffer. This solution was used to dissolve cell extract samples (see below).
The SDS-CZE separation was performed using a Beckman Coulter P/ACE MDQ capillary electrophoresis system (CA, U.S.A.), equipped with a UV-detector operating at 214 nm using a 30 cm coated capillary and the separation buffer of the Beckman Coulter SDS 14–200 kit. The capillary temperature was set at 20°C.
Before each analysis, the 30 cm capillary was rinsed in the reverse direction for 1 min at 20 psi using 0.1 M HCl and subsequently for 3 min at 20 psi with SDS separation buffer. The sample solution was injected for 30 s at 1 psi, followed by forward rinse for 30 s at 0.5 psi of SDS sample buffer/water (1:1). The separation voltage was ramped in 1 min to 9 kV (ground at detector outlet) and held constant for 18 min.
A standard solution of lysostaphin was prepared as follows. From a solution of a known concentration of lysostaphin (ca. 1 mg/mL) 40 μL was pipetted into an Eppendorf vial of 0.5 mL and 120 μL of SDS sample buffer was added. The closed vial was incubated for 30 min at 80°C and subsequently rapidly cooled using ice water. From this solution 80 μL was transferred to the sample vial (of 0.2 mL Eppendorf vial).
For the preparation of samples of cell extracts, the same procedure as that for the standard solution of lysostaphin was followed, except that after cooling in ice water the solution was centrifuged for 5 min at 3000 g to remove any possible traces of precipitated proteins.
Analysis of minerals and trace elements in the basic medium was carried out by ICP-AES (Inductively Coupled Plasma – Atomic Emission Spectrometry) using the Vista Axial ICP of Varian (Palo Alto, CA, U.S.A.). The growth medium sample was prepared for ICP by dry-ashing, dissolved in nitric acid and measured against standards of Ca, Mg, Na, K, P, Fe, Zn, Mn and Cu.
We thank Bert van de Bunt and Fedde Kingma for excellent technical assistance. Furthermore, we thank Andy Lees for critical reading of the manuscript.
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