INTRODUCTION
Lysostaphin (LST) is a glycyl-glycine zinc-dependent endopeptidase natively encoded on the pACK1 plasmid of
Staphylococcus simulans (
1), an environmental competitor of
Staphylococcus aureus. LST is synthesized as a preproenzyme of 493 amino acids, and its pre- (36 amino acids) and pro- (211 amino acids) sequences are removed during and after secretion, respectively. Mature LST is a monomer composed of an N-terminal catalytic domain (132 amino acids), a C-terminal cell wall binding domain (102 amino acids), and a short connecting linker (13 amino acids) between the two (
2). The LST enzyme selectively and efficiently degrades pentaglycine cross-links in the peptidoglycan component of
S. aureus cell walls, ultimately resulting in bacterial lysis and death. Lysostaphin was discovered in the 1960s (
3) and has since undergone various degrees of preclinical development and even small-scale clinical testing by different groups and organizations (
4–8). Early interest in LST as a therapeutic agent waned as a result of ready access to conventional drugs, such as methicillin, but enthusiasm for LST in biomedical applications has been revived due to wide-spread antibiotic resistance and shallow antimicrobial development pipelines (
9).
One barrier to LST clinical applications is the high doses required to eradicate some infections. LST appeared to show good efficacy in an unresponsive leukemia patient suffering from multidrug-resistant staphylococcal pneumonia, multiple abscesses, and cellulitis (
7), but this effect required a 500-mg systemic bolus of enzyme. In another study, nasal carriers of coagulase-positive
S. aureus were shown to be effectively cleared of the pathogen following intranasal LST treatment, but this effect required 2 weeks of 4-times-daily intranasal administration of a 5 mg/ml LST solution (
8). Similar results at similar dosages were obtained in other human studies of nasal carriage clearance (
10,
11). In a murine model of catheter-associated
S. aureus biofilms, systemic LST administration was shown to clear established biofilms during a 4-day treatment regime, and a single prophylactic dose prevented subsequent biofilm formation on indwelling catheters (
12). Extrapolating the effective doses to a human patient, however, would require as much as 16 or more grams of enzyme to be administered over 4 days. Thus, while LST has demonstrated consistent efficacy in animal models and even human studies, translating the effective dosages to wide-spread clinical use will require a particularly efficient production platform.
Toward this end, LST has been produced in a wide range of microbial expression hosts. One source of commercial LST is high-cell-density cultures of the native organism
S. simulans, but the industrial-scale production yields from this system are withheld as proprietary information. Alternatively, expression yields from the bacterial host
Escherichia coli are known to range from 10 to 20 mg/liter (
13–15), and this recombinant platform is also a significant contributor to commercially sourced material. Large-scale LST production for clinical trials has been pursued with the
Lactococcus lactis nisin-induced controlled expression (NICE) system (
16,
17). Expression levels of 100 mg/liter were achieved in large-volume, high-cell-density fermentations, but the final purified yields were only 40 mg/liter (
16). Subsequent process optimization of this system increased bioreactor expression levels to 300 mg/liter (
17), but there remains considerable room for further improvement. Finally, it bears noting that LST has also been expressed in mammalian cells (
18), but no effort was made toward maximizing or even quantifying yields.
Pichia pastoris has proved to be a highly successful heterologous expression host in recent years, with more than 1,000 recombinant proteins expressed as of 2009 (
19). Unlike the aforementioned prokaryotic systems,
P. pastoris has dedicated, high-capacity protein secretion pathways, which greatly simplify both upstream and downstream protein purification (
20). Moreover, as a yeast,
P. pastoris produces no endotoxins, obviating the need for arduous and inefficient endotoxin removal steps prior to biomedical applications (
21). Although
P. pastoris is an attractive recombinant host, the expression of bacterial proteins in these eukaryotic cells can present its own challenges. In this study, two key barriers to high-level LST expression in
P. pastoris were encountered, (i) lack of detectable expression from the wild-type (WT) LST gene and (ii) aberrant glycosylation at one of two internal N-linked consensus sequons. These limitations were addressed by optimizing the gene sequence and the protein sequence, respectively.
MATERIALS AND METHODS
Regents and media.
Primers with standard desalting were ordered from IDT Technologies (Coralville, IA). Enzymes for molecular cloning were purchased from New England BioLabs (Ipswich, MA), as was Remove-iT PNGase F. Commercial LST produced in E. coli was purchased from Sigma (St. Louis, MO). All other reagents and supplies were from VWR Scientific (Philadelphia, PA), unless specifically noted.
Plasmids and strains.
P. pastoris expression vector pPIC9 and P. pastoris strain GS115 were purchased from Invitrogen (Grand Island, NY). S. aureus strain SA113 was from the American Type Culture Collection (Manassas, VA). Clinical isolates of S. aureus (strains 6445, 3425-1, and 3425-3) were the kind gift of Ambrose Cheung (Dartmouth, Hanover, NH).
Design of a synthetic lysostaphin gene (SYN lst).
An artificial gene encoding the wild-type LST enzyme was synthesized to satisfy two general objectives: (i) to substitute codons satisfying the preferred codon usage of
P. pastoris for wild-type codons and (ii) to balance the A+T/G+C distribution of segments with disproportionate A+T content. In the synthetic gene, the majority of codons were replaced by the most preferred codons of
P. pastoris (
22). However, to disrupt long stretches of A+T bases, the second-most-frequent
P. pastoris Thr and Val codons were inserted as needed. Specifically, ACC (14.5% usage) instead of ACT (22.4% usage) was occasionally used for Thr, and GTC (14.9%) instead of GTT (26.9%) was used for Val.
Cloning of lst genes.
The WT
lst gene was amplified from
S. simulans with primers WT-F and WT-R (
Table 1). The SYN
lst gene was synthesized by Shanghai Xuguan Biotechnology Development Company (Shanghai, China) and amplified with primers SYN-F and SYN-R (
Table 1). The chimeric and aglycosylated
lst genes were constructed by splice overlap extension PCR using the primers listed in
Table 1. Briefly, paired 5′ and 3′ fragments of the WT or SYN
lst genes were first amplified using one external primer and one internal primer each, and the resulting fragments were then spliced together in an overlap reaction using external primers. For example, two fragments for the N125Q point mutant (with a change of N to Q at position 125) were generated by amplifying SYN
lst with (i) SYN-F and N125Q-R and (ii) SYN-R and N125Q-F. The resulting PCR products were then mixed at an equimolar ratio, and the mixture was used as the template in a subsequent splicing overlap reaction using primers SYN-F and SYN-R. All PCRs were performed using Phusion high-fidelity DNA polymerase. The LST-encoding genes were digested with XhoI and EcoRI, ligated into similarly digested pPIC9, and transformed by electroporation into
E. coli DH5α [F
− ϕ80
lacZΔM15 Δ(
lacZYA-argF) U169
recA1 endA1 hsdR17 (r
K− m
K+)
phoA supE44 λ
− thi-1 gyrA96
relA1]. This fuses LST in frame with the alpha mating factor (αMF) secretion signal from
Saccharomyces cerevisiae. Clones bearing the expression vector with the insert were selected by PCR using external primers (either WT-F with WT-R or SYN-F with SYN-R) and confirmed by DNA sequencing.
P. pastoris expression.
The pPIC9 expression vectors harboring sequenced lst genes were digested with SacI prior to electroporation into P. pastoris strain GS115. P. pastoris transformants were initially grown on solid MD medium (1.34% yeast nitrogen base [YNB], 0.00004% biotin, 2% dextrose, 1% agar), then cultured in BMGY medium (1.0% yeast extract, 2.0% peptone, 1.34% YNB, 0.00004% biotin, 1.0% glycerol, 100 mM phosphate buffer, pH 6.0), and finally induced in BMMY medium (1.0% yeast extract, 2.0% peptone, 1.34% YNB, 0.00004% biotin, 0.5% methanol, 100 mM phosphate buffer, pH 6.0). LST-expressing clones were identified by SDS-PAGE analysis of culture supernatants.
RT-PCR.
A 5′ fragment or full-length LST mRNA was detected by reverse transcription (RT)-PCR using forward primer WT-F or SYN-F and reverse primer 5WT-R, 5SYN-R, FullWT-R, or FullSYN-R (
Table 1). As an internal positive control, a fragment of alcohol oxidase 1 (AOX1) mRNA was detected with primers AOX1-F and AOX1-R.
Bioreactor culture.
For pilot-scale production of LST,
P. pastoris was cultured in a 2-liter bioreactor as described previously (
23). Briefly, a 3-stage fed-batch culture process was employed. First,
P. pastoris was cultured at 30°C in 1.5 liters of low-salt BSM medium (per liter, 20 ml 85% phosphoric acid, 0.2 g calcium sulfate, 5 g potassium sulfate, 4 g magnesium sulfate-7H
2O, 1 g potassium hydroxide, 30 g glycerol). After the initial glycerol had been exhausted, as identified by a dissolved oxygen spike, the culture density was increased to an optical density at 600 nm (OD
600) of approximately 100 using a constant glycerol feed rate of 15 ml/h for 6 h. Finally, the culture temperature was decreased to 20°C and the expression of lysostaphin was induced by a bolus injection of methanol to a final concentration of 0.5%. A controlled methanol feed was initiated upon full induction of the AOX1 promoter, indicated by a steady decrease in dissolved oxygen concentration with the feeding of methanol. A controlled dissolved oxygen (DO-stat) strategy was then employed to maintain 20% dissolved oxygen by adjusting the methanol feed rate (
24).
Lysostaphin purification.
LST was precipitated from culture supernatants by 25% polyethylene glycol (PEG) precipitation at room temperature, resuspended in 20 mM NaHPO4 buffer, pH 7.5, and bound to a HiPrep SP Sepharose fast flow 16/10 prepacked column that had been equilibrated with the same buffer. Following a 10-column-volume wash with the same buffer, LST was eluted with a 0-to-250 mM NaCl gradient, occurring over 10 column volumes. The purity and concentration of eluted LST was determined by SDS-PAGE gel densitometry, using a standard curve generated with commercially sourced LST.
MIC assay.
The MIC of LST was determined by the microplate method (
25). Using 96-well polystyrene plates, 100-μl aliquots of
P. pastoris culture supernatant were serially diluted in tryptic soy broth (TSB), while 100-μl aliquots of purified LST were serially diluted in phosphate-buffered saline (PBS; 2.7 mM KCl, 1.5 mM KH
2PO
4, 8.9 mM Na
2HPO
4, 136.9 mM NaCl, pH 7.4) supplemented with 0.1% bovine serum albumin. Each well was then inoculated with 100 μl of ∼10
6 CFU/ml
S. aureus strain SA113 in TSB or Mueller-Hinton broth (BD) supplemented with 2% NaCl, yielding a total volume of 200 μl per well. Microplates were then incubated at 37°C for 24 h. The inhibitory activity in culture supernatants was assessed as the MIC
50, the treatment dilution yielding 50% inhibition of growth. The inhibitory activity of purified LST was determined by the MIC
0, the enzyme concentration yielding complete inhibition of growth. Both MIC
0 and MIC
50 were quantified by measuring light scattering at 650 nm in a microplate reader. All assays were performed in duplicate.
Turbidity assay.
S. aureus strain SA113 was cultured overnight in TSB, pelleted by centrifugation, and washed once with PBS. The cells were then resuspended in PBS, and this stock bacterial suspension was aliquoted into replicate wells of a 96-well flat-bottomed polystyrene plate (Nunc 269620) (100 μl, A650 = 0.8 in the plate). Lysis reactions were initiated by adding purified LST to a final concentration of 5 μg/ml using a 12-channel Pipetman. The kinetics of bacterial lysis were followed by measuring the light scattering at 650 nm every minute for a total of 30 min. The activity of the various LST constructs was defined as the time to reach half the starting optical density (TOD50) of the initial bacterial suspension.
Thermostability assay.
The relative thermostability of LST constructs was determined by differential scanning fluorimetry on an Applied Biosystems ABI 7500 fast real-time PCR system, essentially as described previously (
26). Proteins and SYPRO orange were diluted in PBS, and fluorescence was quantified at 1-degree increments from 25 to 94°C.
PNGase F treatment.
One microliter of 10× G7 reaction buffer and 1 μl of Remove-iT PNGase F were added to 8 μl of culture supernatant. The reaction mixture was incubated for 1 h at 37°C, and the reaction products were analyzed by SDS-PAGE.
Saturation mutagenesis of LST residue 125.
LST amino acid 125 was subjected to saturation mutagenesis by splice overlap extension PCR using the SYN
lst gene template and degenerate internal primers (NNK codon, where N = A, G, C, or T and K = G or T) (
Table 1). The 32-member gene library was cloned and transformed into
P. pastoris as described above. Transformants were spread on YPM agar medium (1% yeast extract, 2% peptone, 1% methanol, 1% agar) and incubated at 30°C for 2 days. An overnight culture of
S. aureus strain SA113 was diluted in PBS to an OD
600 of 1.0, and this bacterial suspension was mixed in a 1:10 ratio with molten top agar (0.5 yeast extract, 1% peptone, 1% NaCl, 0.75% agar). The indicating top agar was poured onto the YPM yeast plates, and the plates were incubated at 37°C for 10 h. Yeast clones expressing active enzymes were identified by their characteristic halo or zone of clearance. Halo-forming colonies were picked through the top agar, their cognate
lst genes were amplified with primers SYN-F and SYN-R (
Table 1), and the PCR products were sequenced.
Bioinformatics analysis.
Sequence alignment was performed using ClustalW (
www.ebi.ac.uk/Tools/msa/clustalw2/). Codon analysis was performed using CodonW (codonw.sourceforge.net). The frequency of optimum codons (
Fop) is defined by the formula (number of optimal codons)/(total number of codons). Its values range from 0 (when a gene contains no optimal codons) to 1 (when a gene is composed entirely of optimal codons).
Gene sequence deposition.
The optimized SYN lst gene sequence, encoding the wild-type LST enzyme, has been deposited in GenBank with the accession number KF724949.
DISCUSSION
Because of its lack of endotoxin and high inherent capacity for recombinant protein expression and secretion,
P. pastoris is becoming increasingly attractive as a cost-effective production platform for therapeutic proteins. In some cases, however, biotherapeutic protein expression levels have been found to be low to undetectable (
29). Protein secretion from
P. pastoris is a multiple-step process involving transcription, translation, protein folding, and translocation through the secretory pathway. Any one of these steps may be rate limiting for a given protein target (
30,
31). Thus, while
P. pastoris has numerous advantages for biotherapeutic protein production, obtaining high levels of expression with recalcitrant targets can be a difficult problem.
Gene sequence optimization has been a widely effective measure to increase heterologous protein expression levels in
P. pastoris (
32–36), but the mechanism behind this strategy has seldom been studied. The results presented herein are consistent with prior insights that premature transcription termination may result from short segments of severe nucleotide bias within some native genes (
37–39). Thus, targeted disruption of these regions may represent an efficient and cost-effective strategy for gene optimization compared to the whole-gene synthesis strategy. In the current study, the comparison of expression levels from the WT, WTΔAT, SYN, and SYN+AT constructs indicates that the core 21-bp A+T-rich sequence is necessary but not sufficient for a putative premature transcription termination signal. Notably, replacement of a mere six nucleotides was sufficient to activate expression from the otherwise incompetent WT
lst gene.
Aberrant glycosylation is another frequently encountered barrier to high levels of production of functional proteins from
P. pastoris. As shown here, this is indeed the case for the antibacterial enzyme LST. In most instances, destruction of the glycosylation sequon is accomplished by replacing the N-linked asparagine residue with glutamine, aspartic acid, serine, or alanine (
40–43). In the current study of LST glycosylation, all mutations at the N-linked N125 residue led to significantly decreased enzyme activity, whereas mutations at two adjacent residues (S126 and T127) yielded fully functional aglycosylated variants. The severely compromised activity of the N125 mutants was especially surprising given the fact that residue 125 is thought to be located at the C-terminal end of the catalytic domain, and prior studies of key LST catalytic residues did not identify N125 (
2). Molecular modeling of the LST catalytic domain suggested that substitutions at position 125 caused minimal structural perturbation and affected the peptide backbone even less than mutations at positions 126 and 127 (data not shown). Therefore, an understanding of the strict requirement for an asparagine at position 125 awaits more-specific and in-depth mechanistic and structural analyses. Regardless, the current study demonstrates an unexpected positional constraint for mutations able to disrupt an N-linked glycosylation sequon while maintaining protein function.
It has been shown that transgenic animals expressing LST have enhanced resistance to staphylococcal infections (
44). However, transgenic expression of the native LST enzyme is suboptimal, as aberrant glycosylation was found to abolish its activity (
27). To address this issue, aglycosylated LST variants with decreased activity (such as N125Q) have been used in transgenic animal production (
27,
45). Notably, only animals expressing the highest LST(N125Q) levels were completely resistant to staphylococcal infection. We speculate that the optimized aglycosylated LST variants described here would greatly enhance the utility of LST in transgenic animals, and more generally, we anticipate that other functionally sensitive proteins will benefit from a broadened choice of mutations able to disrupt undesirable N-linked glycosylation sequons.
In conclusion, an efficient high-level-production system has been constructed for LST in the yeast host P. pastoris. By a combination of gene sequence, protein sequence, and bioprocess optimization, expression levels of 500 mg/liter and final purified yields of 250 mg/liter have been obtained in laboratory-scale bioreactors. These high yields and the ease of purification for the secreted, endotoxin-free enzyme should facilitate future development of LST applications, particularly those relating to treating bacterial infections in mammals.