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Staphylococcal (or micrococcal) nuclease or thermonuclease (SNase or Nuc) is a naturally-secreted nucleic acid degrading enzyme that participates in Staphylococcus aureus spread in the infected host. Purified Nuc protein can be used as an exogenous reagent to clear cellular extracts and improve protein purification. Here, a recombinant form of Nuc was produced and secreted in a Gram-positive host, Lactococcus lactis, and purified from the culture medium.
The gene segment corresponding to the S. aureus nuclease without its signal peptide was cloned in an expression-secretion vector. It was then fused to a lactococcal sequence encoding a signal peptide, and expressed under the control of a lactococcal promoter that is inducible by zinc starvation. An L. lactis subsp cremoris model strain (MG1363) transformed with the resulting plasmid was grown in either of two media (GM17v and CDM) that are free of animal compounds, allowing GMP (Good Manufacturing Practice) production. Induction conditions (concentration of the metal chelator EDTA and timing of addition) in small-scale pH-regulated fermentors were optimized using LacMF (Lactis Multi-Fermentor), a home-made parallel fermentation control system able to monitor 12 reactors simultaneously. Large amounts of recombinant Nuc (rNuc) were produced and secreted in both media, and rNuc was purified from GM17v medium in a single-step procedure.
In L. lactis, rNuc production and secretion were optimal after induction by 0.5 mM EDTA in small scale (200 mL) GM17v exponential phase cultures (at an OD600 of 2), leading to a maximal protein yield of 210 mg per L of culture medium. Purified rNuc was highly active, displaying a specific activity of 2000 U/mg.
L. lactis which is widely used as a starter in dairy industries, is also an efficient cell factory for the production and secretion of proteins . i) Proteins produced in this species, which is considered as safe by virtue of its longtime human consumption, should obtain the GRAS (Generally Recognized As Safe) status and be suitable for therapeutical or vaccine applications , in contrast to proteins produced in Escherichia coli from which endotoxin (LPS) has to be removed . ii) In this Gram+ species, the secretion of any heterologous protein fused to an appropriate signal peptide can be easily and efficiently driven by the general export (Sec) pathway , thus avoiding potential intra-cellular toxicity and/or misfolding. iii) In this species, an extracellular protease-free strain (without the unique surface protease HtrA ) is a useful host to avoid protein degradation , whereas in Bacillus subtilis, not all extracellular proteases have been inactivated to date (4 active surface proteases, including the 3 HtrA family members, are remaining in the available mutant strains) [5,6]. iv) Only one major protein, Usp45, is secreted in significant amounts into the medium , thus facilitating downstream purification steps. v) Finally, setting up conditions for protein production in large fermentors should be easy as culture scale-up is linear .
In this context, several gene expression systems have been developed for L. lactis: i) NICE, the most widely used system based on the PnisA promoter and nisRK two-component regulatory system, is induced by nisin ; ii) P170, which is regulated by RcfB, is induced by lactic acid, in particular during the transition to the stationary phase of growth where the pH is low due to lactate accumulation [10,11] (SM Madsen, personal communication), and iii) PZn is tightly regulated by the ZitR repressor in response to extra-cellular Zn2+ levels: it is repressed in a wide concentration range from repletion to toxicity, and induced by starvation [12-14] (Daniel Llull, Olivier Son, Nicolas Trémillon, Sandrine Blanié, Julien Briffotaux, Sébastien Blugeon, Eric Morello, Hélène Rogniaux, Olivier Danot, and Isabelle Poquet: ZitR, a prototype of a new class of zinc responsive repressors in Streptococcaceae, submitted). As an expression system, ZitR-regulated PZn should allow the repression of a potentially toxic heterologous ORF in the presence of Zn2+ (e. g. in a rich medium), and once a sufficient amount of biomass has been obtained, its induction by addition of a chelator agent (e. g. EDTA) [12,14]. To allow protein secretion, expression systems have been combined with several signal peptides: i) that of Usp45 [1,7] ii) that of Exp4 [13,15,16], and iii) several optimized signal peptides (SP310 series) [17,18].
Finally, with the use of all available tools, L. lactis has proved to be an efficient host for the production and secretion of proteins of medical interest, generally in flasks for laboratory studies , but also in small scale (1L) fermentors . Recently, the lysostaphin from Staphylococcus simulans biovar staphylolyticus was successfully produced at the industrial scale (3000 L) in L. lactis using the NICE system. Surprisingly though, this naturally-secreted protein was produced as a recombinant signal peptide-free form that had to be purified from the lactococcal cell extract [8,19].
In the present study, the efficiency of L. lactis as a host for heterologous protein production and secretion, and the ease of protein purification from a lactococcal culture medium were evaluated using the staphylococcal nuclease Nuc [20,21] as a model protein of biotechnological and commercial interest. Nuc is a robust exo- and endo-5'-phosphodiesterase (EC 22.214.171.124) active against both DNA and RNA [22-24]. It can be used for RNA sequencing  and in several applications where nucleic acid removal is desired, like reduction of the viscosity of a cell lysate, improvement of protein purification, and development of in vitro translation systems [26-28]. In S. aureus, Nuc participates in the spread of the bacterial cells in the infected host  as a naturally-secreted enzyme: cleavage of the precursor signal peptide leads to the secretion of the pro-peptide form (NucB) that is processed to the mature form (NucA) . Different forms of Nuc protein have been produced in several species: the native wild-type form, in Bacillus subtilis , Corynebacterium glutamicum  and L. lactis , and recombinant forms fused to different signal peptides, in E. coli [26,34] and in L. lactis [16,35] where NucB processing to NucA was found to require HtrA protease [3,36].
In this study, a recombinant Nuc form (rNuc) was successfully produced and secreted in L. lactis using a recently developed expression-secretion system  and small-scale pH-regulated reactors. An active rNuc protein could be purified in a single step from the culture medium, indicating that secretion is a good method for facilitating the purification of a heterologous protein produced in L. lactis.
pGTP_FZ301 (Figure (Figure1A)1A) is an expression and secretion vector for L. lactis that is derived from pLB145 . pGTP_FZ301 enables any ORF to be cloned as a translational fusion to the lactococcal sequence encoding Exp4 signal peptide [15,16], and the fusion and zitR constitute an operon under the control of the PZn promoter . The cloning of nucB ORF (encoding NucB form) into pGTP_FZ301 resulted in pGTP_FZ301_NucB, and led to the production of a recombinant precursor that is secreted as rNuc (Figure (Figure1B).1B). This recombinant protein was designed because the wild-type Nuc precursor which bears an atypical signal peptide is not efficiently secreted in L. lactis , in contrast to a fusion between NucB and a lactococcal signal peptide .
For rNuc production in L. lactis subsp cremoris strain 918 [MG1363(pGTP_FZ301_NucB)], a new medium was developed. This rich medium is free of animal compounds (GM17v), which could prove useful for the production of proteins that must be devoid of any potentially pathogenic contaminant, such as therapeutic proteins. In pH-regulated cultures using GM17v, a final OD600 of 15-16 could be reached (Figure (Figure22).
The induction parameters of GM17v cultures were optimized taking previously published data about the lactococcal fermentation process  and induction conditions of ZitR-regulated PZn in other media ( and data not shown) into account. Optimization was achieved using LacMF, a parallel fermentation control system able to monitor 12 mini-reactors simultaneously (Additional file 1, Figure S1).
To determine the PZn induction conditions in GM17v, different concentrations of the metal chelator EDTA were added to cultures in different growth phases. Both cell growth and rNuc secretion in the medium were monitored (Figure (Figure2).2). Before induction, the rNuc protein was undetectable in mid-exponential phase cultures (for uninduced cells at an OD600 of 2 or 4, data not shown and Figures Figures2A2A and and2B),2B), and present in low amounts for late-exponential/stationary phase cultures (5 mg/L for uninduced cells at an OD600 of 8, Figure Figure2A).2A). This result suggested that the PZn promoter was first repressed and then progressively induced during growth in GM17v medium, probably because extra-cellular Zn2+ became depleted, as previously observed in another rich medium, GM17 (data not shown), and in a chemically defined medium  (Daniel Llull, Olivier Son, Nicolas Trémillon, Sandrine Blanié, Julien Briffotaux, Sébastien Blugeon, Eric Morello, Hélène Rogniaux, Olivier Danot, and Isabelle Poquet: ZitR, a prototype of a new class of zinc responsive repressors in Streptococcaceae, submitted).
When added at 1 mM at an OD600 of 2 (Figure (Figure2A)2A) or below (data not shown), EDTA impaired growth which stopped as early as one generation after addition. When 1 mM EDTA was added at an OD600 of 4 or 8, the growth impairment seemed to be weaker, probably because late or post-exponential phase cells could almost reach the growth plateau after exposure to the inducer (Figure (Figure2A).2A). The time of induction had a significant effect on the level of rNuc in the medium. Induction before the OD600 reached 2 severely impaired growth and consequently low rNuc levels were obtained (data not shown). In contrast, when EDTA was added at an OD600 of 2 or above, rNuc accumulated rapidly within the first hour of induction, and a high final level of between 100 and 200 mg/L was reached. The optimum of 200 mg/L was obtained for induction at OD600 4 (Figure (Figure2A2A).
In a second phase of optimization, different concentrations of EDTA were added at an OD600 of 2 (Figure (Figure2B).2B). Whereas EDTA at 1 mM (Figure (Figure2A)2A) or above (data not shown) severely impaired growth, little (a slightly reduced OD600 at the plateau) or no growth defect was observed for 500 μM or 100 μM EDTA (Figure (Figure2B).2B). rNuc production in the medium significantly varied with the inducer concentration. After induction with 100 μM EDTA, the rNuc level followed growth and reached its maximum only at the growth plateau, whereas higher EDTA concentrations led a drastic rNuc accumulation within the first hour of induction (Figure (Figure2B)2B) followed by a slight further augmentation afterwards. Interestingly, the fast kinetics of accumulation was not related to a growth defect as it could be observed for either 500 μM EDTA (Figure (Figure2B)2B) or 1 mM EDTA (Figure (Figure2A).2A). 500 μM was found to be the optimal inducer concentration when added at OD600 2 and allowed rNuc production to reach a level of 200 mg/L.
As these results indicated that (i) both time of induction (OD600) and EDTA concentration were important parameters for rNuc production, and that (ii) rNuc continued accumulating untill the growth plateau was reached (albeit sometimes slowly), the combined effect of both parameters on final rNuc levels after prolonged cultures was monitored (Figure (Figure2C).2C). rNuc increased in direct proportion to the EDTA concentration up to 500 μM. Above 1 mM EDTA, rNuc production did not improve regardless of the OD600 at which EDTA was added (Figure (Figure2C).2C). The maximal concentration of rNuc in the medium, 210 mg/L, was obtained when 500 μM EDTA was added to cells at an OD600 of 2 (Figures (Figures2B2B and and2C),2C), thus defining the optimal conditions for rNuc production and secretion in lactococcal cultures grown in GM17v.
In a second set of experiments, two media, the previously-used rich medium, GM17v, and a chemically defined medium, CDM , were compared. Interestingly, the induction conditions optimised for GM17v medium were applicable to CDM and allowed production of rNuc to comparable levels (Figure (Figure33).
rNuc produced and secreted by strain 918 at the highest level (after induction of cells grown in GM17v to an OD600 of 2 by 500 μM EDTA) was purified from the culture medium using a simple, previously-described single step procedure . This procedure, based on cation exchange chromatography, excludes Usp45, the main secreted lactococcal protein  (Figure (Figure4).4). Approximately 85% of rNuc could be recovered from the culture supernatant by this method (data not shown), and finally, ultrapure rNuc (> 99%) concentrated at 115 mg/L (as determined by SDS-PAGE analysis using Bovine Serum Albumin (BSA) as a standard) was obtained. Nuclease activity on denatured DNA was assayed as previously described [22,23], showing that purified rNuc exhibited a high specific enzymatic activity of 2000 U/mg (for comparison, this is 7-20 times higher than a marketed Nuc protein ).
To determine the conditions for the use of L. lactis to produce a secreted heterologous protein, we chose the staphylococcal nuclease, a protein used in the field of biotechnology. This nucleic acid degrading enzyme can be used in several applications, particularly protein purification, by reducing the viscosity of a cell lysate [26,27] and the nucleic acid contamination of the protein which, in the specific case of therapeutic proteins, is required by FDA to be less than 100 pg per dose .
A new system for the production of recombinant proteins was developed. As a cell factory, we used L. lactis grown in either a new, rich and animal compound-free medium (GM17v) or a chemically defined medium (CDM). The heterologous ORF was cloned in pGTP_FZ301 vector under the control of PZn and fused to the sequence encoding the Exp4 signal peptide, and its expression was induced by the chelator EDTA. The whole production-secretion system should be fully compatible with regulatory restrictions in bioproduction for human therapeutics, and the proteins produced with it should be considered as GRAS products. Alternatively, L. lactis grown in CDM medium might also be an interesting host system for specific amino acid labelling (C13, N15, seleno-methionine or seleno-cysteine) and protein structural studies through NMR or X-Ray crystallography.
For cell growth, a pH-regulated batch fermentation process was used. Using a parallel fermentation control system (LacMF), the pH value was maintained at the set point by the addition of a mild alkaline agent, NH4OH. It was previously shown that pH neutralization leads to prolonged exponential growth of L. lactis and increases the final cell density about fivefold compared with pH-unregulated batch culture fermentation [17,19]. Indeed, the biomass of pH-regulated cultures reached high levels (final OD600 of around 15-16, Figures Figures22 and and3).3). NH4OH addition also maintains lactic acid in its dissociated lactate form which is less-toxic  even though at high concentrations, it also slows growth . To further increase the productivity of the expression system used here, lactate [43,44] should be continuously extracted using continuous perfusion  (unpublished results) and electro-dialysis (i. e. REED) . The latter technology with lactococcal expression system P170, allowed to reach protein yields in the gram per liter range . Medium composition could also be optimized, as the addition of nitrogen and carbon sources was previously found to significantly increase protein production in L. lactis grown in a rich medium .
LacMF was a useful tool to optimize EDTA induction in L. lactis. The best way to induce the PZn promoter was to add a non-toxic concentration of EDTA to an exponential phase culture, in agreement with what had previously been observed in another medium . Induction in the exponential phase should maximize the effective production period before the stationary phase and toxic lactate accumulation.
In the absence of induction, rNuc is first undetectable when produced by exponentially growing cells, suggesting that its expression is repressed, and then weakly induced in late-exponential/stationary phase cells (Figures (Figures2A2A and and2B),2B), as previously observed in another medium  (Daniel Llull, Olivier Son, Nicolas Trémillon, Sandrine Blanié, Julien Briffotaux, Sébastien Blugeon, Eric Morello, Hélène Rogniaux, Olivier Danot, and Isabelle Poquet: ZitR, a prototype of a new class of zinc responsive repressors in Streptococcaceae, submitted). This growth-phase dependent regulation suggests that free Zn2+, initially present in the medium at repression levels, could become exhausted or unavailable during growth, thus leading to progressive PZn induction  (Daniel Llull, Olivier Son, Nicolas Trémillon, Sandrine Blanié, Julien Briffotaux, Sébastien Blugeon, Eric Morello, Hélène Rogniaux, Olivier Danot, and Isabelle Poquet: ZitR, a prototype of a new class of zinc responsive repressors in Streptococcaceae, submitted). This could also explain the differences in rNuc accumulation kinetics according to the inducer concentration. When induced at high EDTA concentration (at and above 500 μM), rNuc rapidly accumulates (within 1 h) almost to its maximal level, whereas at 100 μM EDTA, accumulation is much slower and goes on for a longer time (Figure (Figure2B).2B). Interestingly, rNuc levels of exponentially growing cells induced by 100 μM EDTA for 1 h (Figure (Figure2B)2B) and of uninduced cells at OD600=8 (Figure (Figure2A)2A) are similar, suggesting that 100 μM EDTA only has a weak inducing effect, in agreement with the observation that it has only a slight, if any, effect on cell growth (Figure (Figure2B).2B). The final rNuc level after several hours of induction by 100 μM EDTA (Figure (Figure2B)2B) might result from an increased production rate due to a higher biomass in a medium progressively depleted of Zn2+.
The EDTA concentration for optimal induction is significantly higher (more than 10 times) in both GM17v and CDM medium than in SA, the medium we previously used . This is not surprising, as CDM and SA media are highly different, notably for their micro-nutrient composition (for example Mn2+ and Cu2+ are not added to CDM in contrast to SA), and in particular for Zn2+ content, which is much higher (3 orders of magnitude) in CDM than in SA [37,48]. Meanwhile, in both CDM and GM17v medium, the same optimal inducer concentration leads to a similar level of rNuc in the medium. As PZn expression level was recently found to be inversely correlated to extra-cellular Zn2+ concentration (Daniel Llull, Olivier Son, Nicolas Trémillon, Sandrine Blanié, Julien Briffotaux, Sébastien Blugeon, Eric Morello, Hélène Rogniaux, Olivier Danot, and Isabelle Poquet: ZitR, a prototype of a new class of zinc responsive repressors in Streptococcaceae, submitted), this indicated that GM17v and CDM media had similar Zn2+ contents.
Induction by EDTA at high concentration (1 mM) in GM17v and CDM led to a growth defect of strain 918 (Figures 2A, 2B and and3A).3A). However, this was not due to the toxicity of EDTA per se, because of chelation of divalent cations to detrimental levels and cell starvation, as 1 mM EDTA specifically affected strain 918 but not the parental strain MG1363 (under identical conditions in the absence of antibiotic selection; data not shown). The specific growth defect of strain 918 thus seems to result from the presence of the pGTP_FZ301_NucB plasmid, and it is tempting to speculate that it could be due to the metabolic burden of secreted rNuc overproduction. In B. subtilis, a similar inducer-dependent growth defect has already been described for a strain over-expressing an heterologous secreted protein: it was associated to a secretion stress that was shown to lead to an adaptative cell response including the induction of the CssRS regulon [49-51]. This study should help define the conditions for hitherto unexamined secretion stress in L. lactis.
In this study, under optimal induction conditions, an rNuc production yield of 210 mg/L was reached. This yield is comparable to the ones previously obtained for staphylococcal nuclease forms produced in pH-regulated fermentative cultures of L. lactis using inducible P170 promoter  or the constitutive Pusp45 promoter . The efficiencies of the ZitR-regulated PZn and NICE expression systems were found to be comparable under classical conditions . All these comparisons indicate that pGTP_FZ301 is an efficient tool and a useful alternative expression-secretion system in L. lactis.
rNuc could be purified from a lactococcal culture medium in a single-step process. As L. lactis secretes few native proteins, heterologous protein secretion greatly simplifies downstream processing and purification. Indeed, after a single purification using cationic exchange resin, 85% of the rNuc protein was recovered pure at 99% and fully active. For comparison, the cytoplasmic recombinant form of lysostaphin produced in L. lactis using the NICE expression system was recovered to 80%, and was only 90% pure after three steps of cation exchange chromatography . Similarly, the staphylococcal nuclease R produced by E. coli required two steps of metal chelating affinity chromatography to be purified from a cell extract .Thus secretion in L. lactis appears to simplify the downstream purification process.
This study for the first time describes the use of the promoter PZn in pH-regulated mini-reactors. Optimization of induction conditions for nuclease production was rapidly achieved with the use of the pH controller LacMF and allowed to reach a yield of 210 mg/L. Nuclease produced by L. lactis was purified from the culture supernatant, providing a highly pure and active enzyme that should be useful for removing RNA and DNA from cell extracts. The fermentation, production and purification processes that were set up for the production of staphylococcal nuclease in L. lactis proved to be competitive, and they should be used in the future for different heterologous proteins, like proteins of therapeutical value.
E. coli NEB 5-α (New England Biolabs, Ipswich, MA) was grown at 37°C with 200-250 rpm shaking in reconstituted Luria Bertani (LB) broth: 1% tryptone (Sigma, St Louis MO), 5% yeast extract (Fluka, St Louis MO), 1% NaCl (Fluka) resuspended in pure water, supplemented with ampicillin at 100 μg/mL (Sigma) when necessary. Solid media were prepared by adding technical agar (Invitrogen, Paisley UK) at a final concentration of 1.5% w/v. L. lactis MG1363 strain  and strain 918 [i. e. MG1363(pGTP_FZ301_NucB)] were routinely grown at 30°C without shaking in rich M17 (Fluka) supplemented with 1% glucose and with chloramphenicol 5 μg/mL (Sigma) for plasmid selection in the case of strain 918.
LacMF (Additional file 1, Figure S1) is a proportional, integrative and derivative (PID) controller that allows continuous pH monitoring and control of 12 simultaneous mini-reactors of 50 mL-1 L. pH is maintained at the set point by adding 30% v/v NH4OH (Fluka) to the different cultures, using a pump with twelve solenoid valves (Additional file 1, Figure S1) that open sequentially and for limited times. NH4OH neutralizes lactate produced by fermentation, thus impeding medium acidification and leading to prolonged exponential growth and a higher biomass. Cultures are maintained at 30°C and continuously homogeneized by a magnetic stirrer (with 100-150 rpm agitation). LacMF system allowed optimization to be performed quickly, within two weeks and only 4 rounds of 12 independent experiments.
Strain 918 was inoculated to an initial OD600 of 0.2 in 200 mL mini reactors and grown under standard fermentation conditions: at 30°C and pH 6.5 using LacMF. Two different media: a chemically defined medium, CDM , or a rich medium free of animal compounds, GM17v, were used. GM17v contains 1% vegetable extract (Fluka), 0.25% yeast extract (Fluka), 0.05% L-ascorbic acid (Sigma), 1.9% Sodium glycero-phosphate (Sigma), 0.05% MgSO4 (Fluka) and 5% glucose. When necessary, EDTA 0.5 M w/v (Sigma) was added to reach the indicated final concentrations and induce rNuc expression. Samples were harvested every hour to monitor bacterial growth by spectrophotometrically measuring absorbance at 600 nm.
Plasmids used in this study are listed in Table Table11 and cloning strategy is shown in Figure Figure5.5. Sequence coding for Exp4 signal peptide (SPExp4) was amplified from pLB145  in a two-step PCR: using primers 1 and 2 (see Table Table22 for primer sequences) for 5 cycles, and then primers 3 and 4 for 25 cycles. PCR product digested by RsrII and BamHI was cloned into pGTPb_102a cloning vector digested by the same enzymes, and the ligation was used to transform E. coli NEB 5-α. pGTPb_SPExp4 from an ampicillin resistant clone was verified by digestion and sequencing. PZn zitR expression cassette was PCR-amplified from pLB145 using primers 5 and 6. PCR product digested by AvaII was cloned into pGTPb_102a_SPExp4 previously digested by RsrII and dephosphorylated. Ligation reaction was transformed into NEB 5-α competent cells. pGTPb_PZn zitR-SPExp4 from an ampicillin-resistant clone was verified by digestion and sequencing, revealing three silent mutations in zitR sequence. PZn zitR SPExp4 expression and secretion cassette was PCR-amplified from pGTPb_PZn zitR-SPExp4 using primers 7 and 8. PCR product digested by BglII and EcoRI was ligated into pLB145 previously digested by the same enzymes, and the ligation was introduced into L. lactis MG1363 competent cells. pGTP_FZ301 from a chloramphenicol-resistant clone was verified by digestion and sequencing. nucB ORF that encodes the mature secreted part (NucB or pro-Nuc) of staphylococcal nuclease after signal peptide cleavage  was PCR-amplified from pLB145  using primers 9 and 10. PCR product was digested by BamHI and KpnI, cloned into pGTP_FZ301 previously digested by BamHI and KpnI, and ligation was used to transform MG1363. pGTP_FZ301_NucB plasmid extracted from a chloramphenicol resistant clone was verified by digestion and sequencing.
Restriction enzymes, T4 DNA ligase and Antartic phosphatase (New england Biolabs, Ipswich, MA), high fidelity Phusion™ DNA polymerase (Finnzymes, Espoo, Finland) were used according to recommendations. DNA purification kits were purchased from Macherey-Nagel (Düren, Deutschland). Sequencing was performed by Genome express (Meylan, France).
Supernatants were separated from cell samples by centrifugation and stored at -20°C. Protein samples were analysed by SDS-PAGE using gradient (7.5-16.8%) gels and Precision Plus Protein Standards was used for molecular weight estimation (Biorad, California, USA). Commercial BSA (Sigma) was used as a standard for protein quantification. Gels were stained by Coomassie blue G250 (Biorad), scanned (GS800 Calibrated densitometer, Biorad) and analyzed using Image Quant (Amersham Biosciences, Uppsala Sweden).
Culture supernatant was filtrated on 0.22 μm membrane, diluted 15-fold in ultrapure water and loaded on a 10 mL SP sepharose column (GE healthcare, Hillerod, Denmark). All purification steps were performed on an AKTA purifier (GE healthcare). Column was washed with 20 volumes of washing buffer (15 mM sodium phosphate buffer, 15 mM NaCl, pH 7.5). Nuclease was eluted by 10 volumes of elution buffer I (15 mM sodium phosphate buffer, 500 mM NaCl, pH 7.5) and automatically collected in fractions of 2.5 mL using FRAC910 (GE Healthcare). Elution fractions were checked by SDS-PAGE, pooled together and dialysed four times using a Spectra POR dialysis membrane with a cut-off of 3.5 kDa (Spectrum, Rancho Dominguez, CA) against 500 mL of dialysis buffer (20 mM Tris buffer, 100 mM NaCl, 2 mM EDTA, pH.7.5). Nuclease concentration was measured by densitometry and the purified protein was stored at -20°C in storage buffer (10 mM Tris buffer,, 50 mM NaCl, 1 mM EDTA, 50% glycerol, pH 7.5).
Nuclease activity was assayed using a modified version of a previously described method . 10 μL of purified nuclease protein was incubated in 500 μL of reaction buffer (25 mM Tris-HCl, 10 mM CaCl2, 0.01% BSA (w/v), 0.1% Salmon sperm DNA pH 8.8) at 37°C for 30 min, and the reaction was stopped by addition of 500 μL of 4% (v/v) perchloric acid and left for 15 min on ice. In negative controls, purified nuclease protein was added after the addition of perchloric acid. Acid-insoluble nucleic acids were sedimented by centrifugation for 10 min at 15000 g at 4°C. DNA hydrolysis was determined by spectrophotometrically measuring the absorbance of acid soluble polynucleotides at 260 nm (One unit is defined as producing 1 μmole of acid soluble polynucleotides from DNA per minute at pH 8.8 and 37°C ).
The authors declare that they have no competing interests.
NT designed and supervised experiments and drafted the manuscript. NI initiated the experiments. JM and TD respectively supervised purification and fermentation experiments. HG, ED and IP defined the strategy and supervised the project. HG and ED helped to draft manuscript, and IP edited the manuscript. IP supervised the entire PhD project of NT. All authors read and approved the final manuscript.
LacMF, a parallel fermentation control system. 12 lactococcal cultures in mini-reactors of 200 mL can be made in parallel. They are maintained at 30°C and continously homogeneized by a magnetic stirrer ༉), and pH is controlled by supplying a neutralizing agent, NH4OH, via a proportional, integrative and derivative (PID) controller. NH4OH is added to the mini-reactors by a pump () with twelve solenoid valves ().
NT was a recipient of a CIFRE grant between Ministère de l'Enseignement Supérieur et de la Recherche (Paris, France) via ANRT (Association Nationale de la Recherche et de la Technologie, Paris, France) and GTP Technology (Labège, France). We thank Constant Meunier, Corinne Bruand and Carinne Velasco from GTP-Technogy for excellent technical assistance. We are thankful to Maarten van de Guchte (Institut Micalis, INRA, Jouy-en-Josas, France) for critical reading of the manuscript.