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Streptomyces spp. as efficient expression system for a d,d-peptidase/d,d-carboxypeptidase involved in glycopeptide antibiotic resistance



VanYn, encoded by the dbv7 gene (also known as vanY n ) of the biosynthetic cluster devoted to A40926 production, is a novel protein involved in the mechanism of self-resistance in Nonomuraea sp. ATCC 39727. This filamentous actinomycete is an uncommon microorganism, difficult-to-handle but biotechnologically valuable since it produces the glycopeptide antibiotic A40926, which is the precursor of the second-generation dalbavancin in phase III of clinical development. In order to investigate VanYn role in glycopeptide resistance in the producer actinomycete an appropriate host-vector expression system is required.


The cloning strategy of vanY n gene (G-C ratio 73.3%) in the expression vector pIJ86 yielded a recombinant protein with a tag encoding for a histidine hexamer added at the C-terminus (C-His6-vanY n ) or at the N-terminus (N-His6-vanY n ). These plasmids were used to transform three Streptomyces spp., which are genetically-treatable high G-C content Gram-positive bacteria taxonomically related to the homologous producer Nonomuraea sp.. Highest yield of protein expression and purification (12 mg of protein per liter of culture at 3 L bioreactor-scale) was achieved in Streptomyces venezuelae ATCC 10595, that is a fast growing streptomyces susceptible to glycopeptides. VanYn is a transmembrane protein which was easily detached and recovered from the cell wall fraction. Purified C-His6-VanYn showed d,d-carboxypeptidase and d,d-dipeptidase activities on synthetic analogs of bacterial peptidoglycan (PG) precursors. C-His6-VanYn over-expression conferred glycopeptide resistance to S. venezuelae. On the contrary, the addition of His6-tag at the N-terminus of the protein abolished its biological activity either in vitro or in vivo assays.


Heterologous expression of vanY n from Nonomuraea sp. ATCC 39727 in S. venezuelae was successfully achieved and conferred the host an increased level of glycopeptide resistance. Cellular localization of recombinant VanYn together with its enzymatic activity as a d,d-peptidase/d,d-carboxypeptidase agree with its role in removing the last d-Ala from the pentapeptide PG precursors and reprogramming cell wall biosynthesis, as previously reported in glycopeptide resistant pathogens.


Filamentous actinomycetes are high G-C Gram-positive microorganisms commercially widely used as producers of natural products (in particular antibiotics) and industrial enzymes [1]. Genome sequencing of representative microbes belonging to this group has shown that they possess a vast array of genes devoted to the production and secretion of enzymes, due to the role they play in recycling organic material in the biosphere [2]. Genome annotation of Streptomyces coelicolor [3], which is the model system for this microbial group, revealed that it encodes 819 potentially secreted proteins including hydrolases, proteases/peptidases, chitinases/chitosanases, cellulases/endoglucanases, amylases and pectate lyases. Moreover, filamentous actinomycetes are rich of novel enzymatic functionalities since each genome hosts twenty-thirty biosynthetic gene clusters (20–100 kbp each) devoted to the production of chemically diverse bioactive metabolites [1]. Among filamentous actinomycetes, the most studied genus is the Streptomyces one, whose members produce two-thirds of the known antibiotics [4]. Streptomyces spp. are also used as host systems for the production of heterologous proteins and of whole biosynthetic clusters originating from less easy-to-handle actinomycetes, such as those belonging to Nonomuraea, Actinoplanes, Planomonospora, Planobispora, Microbispora genera [1]. These uncommon actinomycetes possess a still-untapped richness of metabolic pathways - and some of them are valuable producers of new drugs - but their exploitation is often limited by the lack of genetic manipulation tools [5, 6].

Streptomyces spp. as heterologous hosts for gene expression and protein production offer some advantages in comparison to Escherichia coli, the preferred cell factory for industrial enzymes and therapeutic proteins [7, 8]. Production and isolation of heterologous proteins from E. coli is often limited by insolubility, citotoxicity, uncorrect folding, aggregation in inclusion bodies and lack of secretion [2]. Secretion capability of Streptomyces spp. may prevent the local accumulation of the over-expressed recombinant proteins, reduce their toxicity to host cells, eventually aid correct folding and favour increased production and purification yields [9]. Heterologous expression is often facilitated when the selected host cells are phylogeneticaly related to the homologous producer. This is due to the similarity of codon usage, compatibility with translation machinery, molecular chaperons, and/or redox state of the cells [2].

We recently started studying the role of genes involved in the biosynthesis, regulation, transport and self-resistance of glycopeptide antibiotics in producing strains which belong to uncommon actinomycetes such as Actinoplanes teichomyceticus producing teicoplanin [10, 11] and Nonomuraea sp. ATCC 39727, which produces A40926 [12]. A40926 is the precursor of the semi-synthetic derivative dalbavancin, which is a second generation glycopeptide currently in phase III clinical development for its improved activity, pharmacokinetics and pharmacodynamics [13]. The dbv cluster, which is a contiguous set of 37 ORFs devoted to the production, regulation and transport of A40926, contains the vanY n gene, whose function was proposed to confer glycopeptide resistance to the producing strain by reprogramming peptidoglycan cell wall biosynthesis [12, 13].

The aim of this work was developing an appropriate heterologous expression system for VanYn characterization to help deciphering its role in glycopeptide resistant cells. Our attention was given to screening different Streptomyces spp. as hosts for recombinant VanYn secretion in biologically active form. Conditions for production (and purification) of functional VanYn were finally successfully settled in Streptomyces venezuelae ATCC 10595 at flask and at fermentor-scale.


Heterologous expression of VanYn in Streptomycesspp

vanY n encoding gene (CAD91202) was amplified by PCR using chromosomal DNA template from Nonomuraea sp. ATCC 39727 [12] and cloned in the multicopy vector pIJ86, under the control of the heterologous constitutive promoter ermE* [14]. The gene was cloned in frame with a sequence encoding for a histidine hexamer added at the C-terminus (C-His6-vanY n ) or at the N-terminus (N-His6-vanY n ) of the protein product.

pIJ86ΩC-His6-vanY n , pIJ86ΩN-His6-vanY n , and the empty pIJ86 used as a control, were introduced in three different Streptomyces spp. by intergeneric conjugation from E. coli. Streptomyces lividans TK24 was selected as one of the hosts since it is used for heterologous protein production due to its proven excellence in secretion capacity and low extracellular protease activity [15]. Streptomyces venezuelae ATCC 10595 is a fast growing streptomyces naturally susceptible to glycopeptides [12]. Streptomyces coelicolor A3(2) represents the model system [3] and possesses a complete set of vanRSHAX genes conferring high resistance to vancomycin: consequently a glycopeptide susceptible mutant deleted in the two component regulatory system ΔvanRS was used in our experiments [16].

Growth curves at shake flask-scale of the ex-conjugants S. coelicolor ΔvanRS, S. lividans and S. venezuelae carrying pIJ86ΩC-His6-vanY n or pIJ86ΩN-His6-vanY n were compared with control strains containing the empty vector in two different cultivation conditions, i.e. by using the limpid YEME medium or the rich and complex BTSB medium (Figure 1 and Table 1). Figure 1A and 1B show the growth curves of S. venezuelae recombinant strains, which produced abundant biomass in both the media. Introduction of vanY n slightly affected biomass productivity. Growth kinetics was similar among S. venezuelae carrying either C-His6-vanY n or N-His6-vanY n constructs and the control strain. Maximum biomass production (≥ 30 g/L dry weight) was achieved after 72 hours from the inoculum in both YEME and BTSB media. Glucose was consumed with different kinetics between the two media, but it was anyhow completely depleted within 72 hours of growth. Observation at the optical microscope showed that mycelium in recombinant strains was more fragmented than in the control one (Figure 1C).

Figure 1

Growth of S. venezuelae pIJ86ΩC-His 6 - vanY n , S. venezuelae pIJ86ΩN-His 6 - vanY n and S. venezuelae pIJ86 in YEME (A) and in BTSB (B) at flask level. S. venezuelae pIJ86ΩC-His6-vanY n dry weight (■ , solid line) and glucose consumption (□, dashed line); S. venezuelae pIJ86ΩN-His6-vanY n dry weight ( , solid line) and glucose consumption (, dashed line); S. venezuelae pIJ86 dry weight (♦, solid line) and glucose consumption (, dashed line). In (C), morphology of S. venezuelae pIJ86 (1), S. venezuelae pIJ86ΩN-His6-vanY n (2) and S. venezuelae pIJ86ΩC-His6-vanY n (3) grown in YEME for 72 hours at the optical microscopic observation (Zeiss Primo Star phase-contrast microscopy with 40X enlargement).

Table 1 Biomass and VanY n production in recombinant Streptomyces spp.

Data in Table 1 shows that S. coelicolor ΔvanRS recombinant strains grew better in BTSB than in YEME, whereas recombinant S. lividans strains did not grow in YEME medium. Different effects of medium composition on growth rate and morphology of suspension cultures (i.e. size of mycelium pellets) among diverse streptomyces hosts have been previously observed [14]. Production of His6-VanYn was evaluated by Western blot analysis after 72 hours of growth in S. venezuelae, S. coelicolor ΔvanRS and S. lividans recombinant strains. In BTSB medium, recombinant VanYn volumetric and specific productivities ranged between 18 to more than 30 mg per liter of culture and from 0.8 to more than 1 mg per gram of cells, within the different recombinant strains. In YEME medium, the highest values of volumetric (about 30 mg of VanYn per liter of culture) and specific (slightly less than 1 mg of enzyme per gram of cells) productivities were achieved only for S. venezuelae recombinant strains. Considering that BTSB medium contains complex components which may later on interfere with protein purification, YEME medium was preferred for large-scale protein preparation. Accordingly, S. venezuelae was selected as the preferable host for protein production scaling-up and purification.

Cellular localization of His6-VanYn was analyzed after 72 hours of growth in S. venezuelae, S. coelicolor ΔvanRS and S. lividans recombinant strains by Western blot analysis on different fractions (prepared as described in the Methods section). Figure 2A shows a ~ 25 kDa band corresponding to His6-VanYn (predicted molecular mass of native VanYn is 22.1 kDa) in the insoluble and soluble cell-free fractions and in the cell wall fractions from S. venezuelae recombinant strains grown in YEME medium. Recombinant VanYn was never found in the concentrated broths (extracellular fractions, lanes 1 and 5 of Figure 2A). Densitometric analysis demonstrated that His6-VanYn preferentially accumulated (90%, lanes 4 and 8 of Figure 2B) in the cell wall fractions obtained by the step of spheroplast preparation, independently on the localization of the His6-tag (at the C-terminus or at the N-terminus of the protein). Only 6% and 4% of recombinant protein was detected in insoluble and soluble cell-free fractions following spheroplast burst, respectively. For all recombinant strains grown in BTSB or YEME (Table 1), the heterologous protein distribution was exactly as for S. venezuelae, with most of VanYn recovered from the cell wall fraction (data not shown).

Figure 2

Western blot analysis of C-His 6 -VanY n and N-His 6 -VanY n from S. venezuelae recombinant strains. (A): analysis of samples corresponding to cellular and extracellular fractions from cultures of S. venezuelae recombinant strains grown in YEME for 72 hours. From S. venezuelae pIJ86ΩN-His6-vanY n : extracellular fraction (lane 1), soluble cell-free fraction (lane 2), insoluble cell-free fraction (lane 3) and cell wall fraction (lane 4); from S. venezuelae pIJ86ΩC-His6-vanY n : extracellular fraction (lane 5), soluble cell-free fraction (lane 6), insoluble cell-free fraction (lane 7) and cell wall fraction (lane 8). A crude extract from S. venezuelae cells carrying the empty vector was loaded as a negative control (CTRL). In each lane, samples corresponding to 100 μL of cell culture were loaded. Std reference protein: C-His6-VanYn from E. coli (5 μg, 25 kDa). The corresponding SDS-PAGE is shown in the Additional file 1: Figure S1. (B): quantitative analysis of recombinant VanYn present in each fraction, performed using the Quantity One program (Bio-Rad Laboratories, Milan, Italy) and His6-VanYn as comparative standard. Total protein content in each fraction was determined by Biuret method (□, solid line).

VanYn production by S. venezuelaein 3 L bench-bioreactor scale

Both the forms of recombinant His6-VanYn were produced growing S. venezuelae recombinant strains in YEME medium at 3 L bench-bioreactor scale. Figures 3A, B and C show the time course of growth and VanYn production of S. venezuelae carrying pIJ86ΩC-His6-vanY n . Exponential growth was actually completed within 48 hours and gave a maximum biomass yield of 40 g/L dry weight. This growth phase was accompanied by a complete depletion of glucose from the medium and by a transient reduction of dissolved oxygen (pO2). Medium pH slightly decreased during the exponential growth phase and then tended to increase during the stationary growth phase. An estimated maximum of production of ~ 30 mg VanYn/L in the crude extract was determined at the peak of biomass production, i.e. at 48 hours from inoculum. An overlapping profile of growth curve and VanYn production was similarly obtained for S. venezuelae carrying pIJ86ΩN-His6-vanY n (not shown).

Figure 3

Growth curve and VanY n production in 3-L batch fermentations of S. venezuelae pIJ86ΩC-His 6 - vanY n in YEME. (A) Time courses of pH (□, dashed line), pO2 (, solid line), glucose (, dashed line), and growth curve measured as dry weight (♦, solid line). (B) Time course of recombinant VanYn production as determined by quantitative Western blot analysis of crude extracts from cell samples collected at different times of fermentation (see panel C). Maximum protein expression at 48 hours of growth was set as 100% (corresponding to ~ 30 mg/L of culture). Total protein content in each fermentation sample was determined by Biuret method ( , solid line). In (C), samples corresponding to 100 μL of cell culture were loaded in each lane; Std, standard reference protein: C-His6-VanYn from E. coli (5 μg, 25 kDa). The corresponding SDS-PAGE is shown in the Additional file 2: Figure S2.

VanYn purification from S. venezuelae

Purification of both the recombinant forms of His6-VanYn from S. venezuelae cells grown in YEME medium, was attempted by means of metal-chelating chromatography on HiTrap chelating column of crude extracts obtained by whole cell sonication, as described in the Methods section. N-His6-VanYn was eluted following standard procedures. In the same conditions, C-His6-VanYn did not bind to the column, suggesting that the six histidines at C-terminus were masked. Accordingly, a denaturing agent such as urea was added to both the loading and equilibration buffers. The partially denatured C-His6-VanYn protein interacted with the matrix and was subsequently re-folded directly on the column by a linear gradient of decreasing urea concentration. SDS-PAGE analysis (Figure 4) confirmed that both the tagged forms of His6-VanYn migrated as a single band of 25 kDa and were > 90% pure. Final purification yield was comparable between the two forms: approximately 12 mg of C- or N-His6-VanYn protein from one liter of culture were recovered.

Figure 4

Purification of recombinant VanY n . SDS-PAGE Analysis (staining with Coomassie brilliant blue) of protein samples collected during purification of VanYn from S. venezuelae carrying pIJ86ΩN-His6-vanY n or pIJ86ΩC-His6-vanY n . Crude fractions from S. venezuelae carrying pIJ86ΩN-His6-vanY n (lane 1) and S. venezuelae carrying pIJ86ΩC-His6-vanY n (lane 2). Fractions from HiTrap Chelating chromatography: N-His6-VanYn flow through (lane 3), C-His6-VanYn flow through at 6 M (lane 4), 4 M (lane 5) and 1 M (lane 6) urea. Purified N-His6-VanYn (lane 7, 2 μg) and C-His6-VanYn (lane 8, 4 μg) after desalting gel permeation. The purified VanYn migrated as a single band at a molecular mass of ~ 25 kDa and with > 90% purity. Standard reference protein: C-His6-VanYn from E. coli BL21(DE3) Star (5 μg, 25 kDa). LMW, molecular mass standard proteins (Amersham, GE-Healthcare).

Enzymatic activity of pure recombinant VanYn

Activities of purified C-His6-VanYn and N-His6-VanYn from S. venezuelae recombinant strains were assayed on commercially available surrogates of peptidoglycan precursors, in parallel with the previously characterized C-His6-VanYn produced by recombinant E. coli [17]. These results were obtained by the d-amino acid oxidase/peroxidase colorimetric coupled reaction [18, 19], and confirmed by a fluorimetric assay [20]. As shown in Table 2, C-His6-VanYn from S. venezuelae cleaved the last d-Ala from the tripeptide Nα,Nε-diacetyl-l-Lys-d-Ala-d-Ala and acetyl-l-Lys-d-Ala-d-Ala, this activity being only slightly affected by the acetylation grade of the Lys. The activity was halved if the substrate was the d-Ala-d-Ala. Thus, C-His6-VanYn showed a higher d,d-carboxypeptidase activity (VanY-like) than a d,d-peptidase activity (VanX-like). Surprisingly, N-His6-VanYn from S. venezuelae did not show any activity on the three substrates (Table 2), suggesting that the tag position dramatically influenced enzyme competence.

Table 2 Substrate specificity of His 6 -VanY n recombinant forms produced by different hosts

These results were supported by the circular dichroism (CD) spectra of the recombinant proteins. CD spectrum of C-His6-VanYn produced in S. venezuelae overlapped with that of the protein produced in E. coli (Figure 5): analysis of secondary structure indicates a predominance of β-sheets (~ 38%) and ~ 15% of α-helices. This structure content was altered for the N-His6-VanYn (Figure 5), indicating that N-terminal tag interfered with the proper protein folding and secondary structure content of the recombinant enzyme.

Figure 5

Far-UV CD spectra of recombinant VanY n . C-His6-VanYn (dotted line) and N-His6-VanYn (dashed line) from recombinant S. venezuelae (S. v.); C-His6-VanYn from recombinant E. coli (E. c.) (continuous line). Protein concentration was 0.1 mg/mL, 15°C.

Resistance phenotype in S. venezuelaerecombinant strains

Role of different constructs of vanY n , when over-expressed in a glycopeptide-susceptible heterologous host such as S. venezuelae, was investigated in vivo by determining the d,d-peptidase/d,d-carboxypeptidase activity of alkaline cell extracts and the glycopeptide resistance phenotype of recombinant strains. As shown in Table 3, d,d-peptidase/d,d-carboxypeptidase activity was detectable only in S. venezuelae pIJ86ΩC-His6-vanY n and S. venezuelae pIJ86ΩvanY n (a strain with vanY n cloned without any tag, see [12]), but not in S. venezuelae pIJ86ΩN-His6-vanY n neither in S. venezualae wild-type or in S. venezualae containing the empty vector. Table 3 also reports the minimal inhibitory concentrations (MICs) of vancomycin and teicoplanin to the recombinant strains in comparison with the wild-type. Accordingly to the expression of the d,d-peptidase/d,d-carboxypeptidase activity, S. venezuelae expressing C-His6-VanYn and S. venezuelae producing VanYn without any tag showed an increased resistance level against both glycopeptides. Resistance phenotype of S. venezuelae producing the N-His6-VanYn was the same as in the control strain with empty vector or in the wild-type.

Table 3 Resistance and enzyme activity profiles of S. venezuelae strains

These data confirm the role of VanYn in conferring glycopeptide resistance to a susceptible host and indicate that C-terminal His6-VanYn behaved in vivo as the native VanYn, whereas the addition of His6 at the N-terminus of the protein abolished its biological activity.


C-His6-VanYn was previously produced in BL21(DE3) Star E. coli cells as a cytoplasmatic soluble protein [13]. In that case, codon usage optimization of the synthetic gene was essential since E. coli is a low G-C ratio (~ 50%) Gram-negative bacterium whereas Nonomuraea sp. is a high G-C Gram-positive actinomycete. The G-C ratio of vanY n is 73.3% which is similar to the genomic ratio of the reference S. coelicolor A3(2) (72%) and S. venezuelae ETH14630 (71%) [14]. The G-C ratio of the dbv cluster is 70.4%. Notwithstanding our efforts in optimizing cultivation, induction and purification conditions, the best productivity achieved in recombinant E. coli was 4.6 mg/L culture (0.13 mg/g cells) [17]. Similar level of expression was obtained by other authors who cloned vanXY C from Enterococcus gallinarum BM4174 in E. coli JM83 [21], vanX from Enterococcus faecium BM4147 in E. coli W3110 [22] and vanY from Enterococcus faecium BM4147 in E. coli JM83 [20]. VanXYC, VanX and VanY are d,d-carboxypeptidases/d,d-peptidases homologous to VanYn involved in conferring glycopeptide resistance to enterococci, which are Gram-positive pathogens with low G-C content [23, 24].

By cloning vanY n from Nonomuraea sp. ATCC 39727 in the taxonomically closely related S. venezuelae, pure protein production was at least three folds higher (12 mg/L culture) than in E. coli. Since estimated volumetric productivity in the harvested cells was around 30 mg of protein per liter of culture, there is still room to improve the final yield by further optimization of the purification procedure. Estimated specific productivity of around 1 mg VanYn per gram of cells in streptomycetes was much higher than the one achieved in E. coli (0.13 mg/g cells) confirming that streptomycetes are preferable hosts for VanYn production. Comparable biomass and protein production were achieved at flask and at 3 L bioreactor-scale: maximum values being one day anticipated in bioreactor runs. Fermentation and downstream technologies are well developed for streptomycetes, which are industrially relevant microorganisms producing many valuable antibiotics and other bioactive metabolites [1]; thus they can be successfully further applied to improving and scaling-up VanYn production.

An important difference between heterologous production of VanYn in recombinant streptomycetes and E. coli is the preferential subcellular localization of the protein. VanYn (196 amino acids) contains three different putative domains: a cytoplasmatic domain at the N-terminus (the first 20 amino acids), an hydrophobic trans-membrane portion (20 amino acids), followed by the C-terminal domain exposed on the external face of cytoplasmatic membrane. This extracellular domain contains conserved motifs (SxHxxGxAxD and ExxH) for the coordination of zinc ions and the catalytic active site [23, 25, 26]. In E. coli recombinant cells, C-His6-tagged-VanYn was accumulated in the cytoplasm, whereas in streptomycetes the most (90%) of the tagged enzyme was recovered from the cell wall fraction. The localization of VanYn confirms its role in the extracellular phases of cell wall biosynthesis [23, 25]. The addition of detergents did not improve purification from the whole cell extract, confirming that the protein is easily detached from membranes. VanY d,d-carboxypeptidases from glycopeptide resistant enterococci are in fact involved in the extracytoplasmatic hydrolysis of the last d-Ala from the UDP-pentapeptide PG precursors [20].

The enzymatic activity and the spectral investigation (by CD spectroscopy) confirmed the identity of C-His6-VanYn produced by recombinant cells of either S. venezuelae or E. coli. On substrates that mimic peptidoglycan precursors, VanYn showed d,d-carboxypeptidase and d,d-dipeptidase activity, resembling more VanXYC from VanC-type Enterococcus gallinarum [21] than typical VanY d,d-carboxypeptidases and VanX d,d-peptidases firstly characterized in Enterococcus faecium BM4147 [20, 27, 28]. On the other hand, the introduction of an histidine hexamer at the N-terminus of VanYn abolishes the enzymatic activity and alters protein secondary structure, suggesting that it interferes with the folding of the active protein. Till now, VanY family of d,d-carboxypeptidases have not been structurally investigated. The possibility to produce discrete amounts of pure VanYn by using S. venezuelae as a cell factory open the way to better investigate the peculiar bifunctional activity of this d,d-dipeptidase/d,d-carboxypeptidase and its interaction with substrates and inhibitors.

Finally, the functional study of recombinant VanYn activity in cellular extracts confirmed the role of this protein in conferring glycopeptide resistance in a susceptible host such as S. venezuelae, which lacks those vanRSHAX genes commonly considered essential to confer glycopeptide resistance [24]. Our data show that when vanY n gene was produced in the biologically active form (C-His6-VanYn or VanYn without any tag), its expression conferred resistance in the absence of vanRSHAX genes, albeit at a reduced level, as previously demonstrated in the homologous producer Nonomuraea sp. ATCC 39727 [12]. As proof of this, expression of the inactive N-His6-VanYn form did not increase the level of resistance towards two glycopeptides (vancomycin and teicoplanin) of the recombinant hosts, which remains the same as in the wild-type and as in the control recombinant strain containing only the empty vector.


Streptomyces spp. were demonstrated valuable hosts for the production of specific peptidases, involved in cell wall turnover of glycopeptide resistant microbial cells. The novel d,d-dipeptidase/d,d-carboxypeptidase VanYn from the glycopeptide producer Nonomuraea sp. ATCC 39727 was successfully produced in a good yield and in the biologically active form conferring resistance to the glycopeptide susceptible S. venezuelae strain. Developing such streptomyces cell factory system for VanYn production opens the way to a further characterization of the enzyme, to a better comprehension of its role in glycopeptide resistance, and to its use as novel biocatalyst.


Strains and media

Nonomuraea sp. ATCC 39727 was maintained and cultivated to prepare genomic DNA according to [12]. Streptomyces coelicolor ΔvanRS was gently donated by Hee-Jeon Hong, University of Cambridge, UK [16], Streptomyces lividans TK24 and Streptomyces venezuelae ATCC 10595 were a gift from Mervyn Bibb, John Innes Institute, Norwich, UK [14]. Streptomyces spp. strains were maintained as spores in 10% (v/v) glycerol and propagated in MYM and SFM agar media [14]. For growing ex-conjugants containing pIJ86, pIJ86ΩC-His6-vanY n , pIJ86ΩN-vanY n and pIJ86ΩvanY n , agar plates were added with 50 μg/mL of apramycin (Sigma-Aldrich, Milan, Italy). Agar plates were incubated at 28°C. Liquid media for streptomycetes were YEME -containing in (w/v) 0.3% yeast extract, 0.5% bacto-peptone, 0.3% oxoid malt extract, 1% glucose in deionized water, pH 7.0- and BTSB -containing in (w/v) 10% sucrose, 1% yeast extract, 1% glucose, 0.5% NaCl, 0.5% soybean meal, 1.7% tryptone and 0.25% K2HPO4 in deionized water, pH 7.0. All medium components were from Sigma-Aldrich (Milan, Italy), unless otherwise stated. Colonies were picked up from agar plates and inoculated into 300 mL baffled flasks containing 50 mL of YEME or BTSB. Flask cultures were incubated on a rotary shaker at 200 rpm and 28°C. Media and culture conditions for E. coli were described in [12]. E. coli DH5α was used as host for plasmid construction. Escherichia coli ET12567/pUZ8002 [5] was used as non-methylating plasmid donor strain for intergeneric conjugation with Streptomyces spp. Cells were propagated in Luria-Bertani (LB) (Sigma-Aldrich, Milan, Italy) broth at 37°C.


pIJ86 (gift from Mervyn Bibb) was used as a multi-copy vector for heterologous expression in Streptomyces spp. [12]. Plasmids pIJ86ΩC-His6-vanY n and pIJ86ΩN-His6-vanY n were constructed as follow. Expand High Fidelity polymerase (Roche, Milan, Italy) was used to amplify vanY n using genomic DNA of Nonomuraea sp. ATCC 39727 as template with oligonucleotide primers vanY004Fw (5-ATAGGATCCCCAGACTGGAGGAGAGGGATGAGGAGAAGCGAGGGTGAC-3) and vanY004Rev (5-GATAAGCTTCTAGTGGTGGTGGTGGTGGTGGACCCGGCCCCCGTTCCGGCT-3) that introduced a C-terminal tag of six histidine residues and the HindIII and BamHI (Roche, Milan, Italy) restriction sites, respectively, into the PCR product, allowing insertion into the multiple cloning site of the multicopy expression vector pIJ86. The vanY n with a N-terminal tag of six histidines was produced using as oligonucleotide primers vanY003Fw (5-ATATTTGGATCCATGCACCACCACCACCACCACAGGAGAAGCGAGGGTGACGAC-3) and vanY003Rev (5-GATAAGCTTCCCGTGCCCTAGCTAGACCCGGCCCCCGTTCCGGCT-3) that introduced HindIII and BamHI restriction sites. The vanY n without any tag was produced using as oligonucleotide primers vanY86Fw (5-ATGGATCCCAGACTGGAGGAGAGGGATG-3) and vanY86Rev (5-GATAAGCTTCGATCCTGGAGTTCGTCTTC-3) that introduced BamHI and HindIII restriction sites [12]. The PCR products were purified, digested with HindIII and BamHI, and ligated with pIJ86 vector that had similarly been digested, to produce pIJ86ΩC-His6-vanY n , pIJ86ΩN-His6-vanY n and pIJ86ΩvanY n . These vectors with vanY n transcribed from the strong constitutive ermE* promoter [14] were used to transform E. coli ET12567/pUZ8002 cells.

Intergeneric conjugation

Intergeneric conjugation was performed according to a modified protocol from [5, 14]. In brief, a culture of the donor E. coli ET12567/pUZ8002 containing the selected plasmid was grown in 10 mL LB supplemented with 50 μg/mL apramycin, 25 μg/mL chloramphenicol (Sigma-Aldrich, Milan, Italy) and 50 μg/mL kanamycin (Sigma-Aldrich, Milan, Italy) to an OD600nm of 0.4. Cells were collected by centrifugation, washed twice with an equal volume of LB, and resuspended in 1 mL of LB. For each conjugation approximately 108Streptomyces spp. spores, collected from agar plates in sterile glycerol, were added to 500 μL 2X YT broth [14], heat shocked at 50°C for 10 minutes and then allowed to cool. 500 μL of E. coli cells were added to 500 μL of heat-shocked spores and mixed briefly. Mixture was plated out on SFM or MYM agar added with 10 mM MgCl2 and incubated for 20 hours at 30°C. Plates were overlaid with 1 mL of water containing 500 μg/mL nalidixic acid (Sigma-Aldrich, Milan, Italy) and 50 μg/mL apramycin and were incubated at 30°C until colonies appear.

Colony PCR and sequencing

The presence of pIJ86ΩvanY n , pIJ86ΩC-His6-vanY n or pIJ86ΩN-His6-vanY n was checked by colony PCR and DNA sequencing of ex-conjugants. Single colonies were transferred onto DNA medium [14]. Plates were incubated at 30°C overnight. Mycelium was scraped from the plates using a sterile toothpick and was introduced into 50 μL 100% v/v DMSO in a 1.5 mL tube. The tube was shaken vigorously for 1–2 hours and then centrifuged: 2.5 μL of the supernatant were used for PCR. For control, 1 μL of DNA samples were mixed with 1.5 μL DMSO. One initial step of 10 minutes at 95°C was included in the PCR program to ensure the complete cell lysis. The PCR was performed for 30 cycles as follows: 95°C for 45 seconds, 56°C for 30 seconds and 72°C for 1 minute. vanY004Fw, vanY004Rev, vanY003Fw and vanY003Rev, vanY86Fw and vanY86Rev were used as oligonucleotide primers.


Recombinant Streptomyces spp. were grown aerobically in 100 mL YEME and BTSB media added with apramycin (50 μg/mL) in 500 mL Erlenmayer flasks for different time intervals (up to 196 h) at 28°C and 200 rpm. Cells were collected by centrifugation at 39000 × g for 15 minutes and washed three times with water. The supernatant (named “extracellular fraction”) was collected and precipitated with the trichloroacetic acid (TCA) method. TCA precipitation was performed adding 1/10 (v/v) of 100% TCA (w/v) to an appropriate medium volume and vortexed for 15 seconds, placed on ice for 15 minutes and then centrifugated at 14,000 × g for 10 minutes. The supernatant was removed and discarded. The pellet was washed twice with 100 μL of pure acetone and then air dried for about 60 minutes.

Washed cells were suspended in 10 mL of 0.1 M Tris–HCl buffer (pH 7.6) containing 0.4 M sucrose and 6.7 mg of lysozyme (Sigma-Aldrich, Milan, Italy). After 6 hours of incubation at 37°C, the mixture was centrifuged at 12800 × g for 10 minutes, obtaining spheroplasts clearly distinguishable at the optical microscopic observation (40X, Zeiss Primo Star microscope, Arese, Italy). The supernatant thus obtained was named “cell wall fraction”. The spheroplasts were washed with 0.4 M sucrose and then 5 mL of water was added to burst the spheroplasts. The suspension was centrifuged at 2000 × g for 30 minutes. The supernatant and the precipitate were named as “cell-free soluble extract” and “cell-free insoluble fraction”, respectively.

Scale up in 3-L reactor

Flask cultures of recombinant Streptomyces spp. grown in YEME and apramycin (50 μg/mL) for 48–72 hours were used to inoculate - at 2.5% (v/v) - 3-L P-100 Applikon glass reactor (height 25 cm, diameter 13 cm) equipped with a AD1030 Biocontroller and AD1032 motor, containing 2 L YEME and apramycin (50 μg/mL). Cultivations in fermenter were carried out for 168 hours at 28°C, with stirring at 500 rpm (corresponding to 1.17 m/s of tip speed) and 2 L/min aeration rate. Dissolved oxygen (measured as % of the initial pO2 value) was monitored using an Ingold polarographic oxygen electrode. The pH values of culture broths were monitored using a pH meter. Foam production was controlled by adding Antifoam SE-15 (Sigma-Aldrich, Milan, Italy) through an antifoam sensor.


For protein purification, cultures of recombinant S. venezuelae grown in YEME medium were harvested and centrifuged at 39000 × g for 15 min at 4°C. Cells were sonicated in a buffer solution 300 mM NaCl, 30 mM imidazole, 10 μg/mL DNAseI (Sigma-Aldrich, Milan, Italy), 0.19 mg/mL PMSF (Sigma-Aldrich, Milan, Italy) and 0.7 μg/mL pepstatine (Sigma-Aldrich, Milan, Italy) in 50 mM potassium phosphate buffer (pH 7.0), for 15 cycles of 30 seconds each on ice. After a centrifugation at 39000 × g for 60 min at 4°C, the supernatant was collected. N-His6-VanYn was purified by affinity chromatography onto a HiTrap chelating affinity column (1.6 × 2.5 cm, 5 mL, GE Healthcare Sciences, Milan, Italy) equilibrated with 50 mM potassium phosphate buffer (pH 7.0) containing 30 mM imidazole and 300 mM NaCl, according to the manufacturer’s instructions. After extensive washing, the bound protein was eluted with 50 mM potassium phosphate buffer (pH 7.0) containing 300 mM NaCl and 300 mM imidazole [17]. For C-His6-tagged VanYn, 6 M urea was added to the equilibration buffer as denaturant; in order to refold the protein bound to the column, a linear gradient from 6 to 0 M of urea (2 mL/min) was performed before starting the elution phase [29]. Fractions containing pure recombinant VanYn were loaded on PD10 Sephadex G25 column (Ge Healthcare Sciences, Milan, Italy) equilibrated with 50 mM potassium phosphate buffer (pH 7.0). Protein purity was checked by SDS-PAGE (using 15% polyacrylamide gels and staining with Coomassie brilliant blue) and Western blot analysis. Protein concentration was estimated using the extinction coefficient at 280 nm (45258 M-1 cm-1) determined by urea denaturation and the theoretical extinction coefficient based on amino acid sequence.

Western blot analysis

Following electrophoresis of proteins from bacterial cell fractions (corresponding to 100 μL of culture) or affinity-purified fractions and the transfer to a nitrocellulose sheet (GE Healthcare Sciences, Milan, Italy), the membrane was incubated with 1:1000 (v/v) His•Tag® Antibody HRP Conjugate Kit (Novagen, Milan, Italy) in alkalin-casein solution 1% (v/v). The immunorecognition was visualized by ECL Detection Reagents (GE Healthcare Sciences, Milan, Italy). The quantitative analysis was performed using the bioinformatics program Quantity One (Bio-Rad Laboratories, Milan, Italy) and C-His6-VanYn from E. coli as standard protein. For molecular mass determination, PageRuler™ Prestained Protein Ladder (Thermo Scientific, Milan, Italy) markers were used. Protein content in each fraction was assayed by Biuret method and SDS-PAGE analysis (Additional file 1: Figure S1 and Additional file 2: Figure S2).

Alkaline extraction of d,d-carboxypeptidase

All manipulations were carried out at 0 to 4°C. Cells at different growth phases were harvested and suspended in 2 ml per gram of cells of physiological solution (0.9% (v/v) NaCl). The mycelium was fragmented by mild sonication and cells were collected by centrifugation at 39,000 × g for 15 minutes. Alkaline extractions were carried out by suspending the cell suspension in ice-cold distilled water containing the proteinase inhibitors (0.19 mg/ml PMSF (Sigma-Aldrich, Milan Italy) and 0.7 μg/ml pepstatine (Sigma-Aldrich, Milan Italy) and then bringing the suspension to pH 12 by adding an appropriate volume of 2.5 N NaOH. After centrifugation (28,000 × g, 15 min, 4°C), the supernatants were neutralized to pH 7 by the addition of 0.5 M sodium acetate (pH 5.4) [30].

d,d-dipeptidase and d,d-carboxypeptidase assays

Enzyme activity was assayed by measuring the release of d-Ala from Nα,Nε-diacetyl-l-Lys-d-Ala-d-Ala, acetyl-l-Lys-d-Ala-d-Ala and d-Ala-d-Ala by a d-amino acid oxidase/peroxidase coupled colorimetric assay (i) or by reaction with a fluorescent reagent (ii). All substrates were purchased from Sigma-Aldrich. One unit of d,d-carboxypeptidase activity was defined as the amount of enzyme that produced 1 μmol of d-Ala per min.

  1. (i)

    D-Amino acid oxidase/peroxidase assay [17, 18]. Reaction mixtures contained 10 mM of the substrate (Nα,Nε-diacetyl-l-Lys-d-Ala-d-Ala, or acetyl-l-Lys-d-Ala-d-Ala or d-Ala-d-Ala), 5 mM of the peroxidase colorimetric substrate 4-aminoantipyrine (4-AAP, from Sigma-Aldrich, Milan, Italy), 3 U/mL RgDAAO (d-amino acid oxidase from Rhodotorula gracilis [18]), 7.5 U/mL horseradish peroxidase (HRP from Sigma-Aldrich, Milan, Italy), 6 mM phenol in 50 mM 1,3-bis[tris(hydroxymethyl)methylamino]propane (pH 7.4) in a final volume of 1 mL. At 25°C, 40 μg of recombinant VanYn or the amount of cell wall alkaline extract correspondent to 50 mg of cells, or the soluble fraction or the supernatant, was added to the reaction mixture and the increase in absorbance (ΔAbs/min) at 510 nm was measured for the test sample as well as for the control to which no VanYn was added. A molar extinction coefficient for chinonemine of 6.58/mM cm was used.

  2. (ii)

    Fluorimetric o–phthaldialdehyde (OPTA) method [20]. Reaction mixtures contained 10 mM Nα,Nε-diacetyl-l-Lys-d-Ala-d-Ala, 40 μg of recombinant VanYn in 50 mM phosphate buffer (pH 7.0) in a final volume of 200 μL. After 10 minutes at 25°C, the reaction was stopped by adding 50 μL of 250 mM HCl followed by 750 μL of water. Enzymatically released d-Ala was detected by the addition of 100 μL of fluoraldehyde (OPTA) solution (Sigma-Aldrich, Milan, Italy) to 100 μL of the reaction mix, followed by incubation at room temperature for 5 min. 800 μL of water was added and 200 μL was removed: the fluorescence intensity was measured (λex = 340 nm; λem = 455 nm) in a fluorescence microplate reader (Tecan Infinite® 200 Pro, Milan, Italy). Assays were quantified from a standard curve prepared with known amounts of d-Ala.

Circular dichroism measurements

Far-UV CD spectra were recorded with a Jasco J-715 (Jasco Europe, Cremella, Italy) spectropolarimeter in the 195–250 nm wavelength range. Measurements were made in quartz cuvettes of 1 mm pathlength, employing protein solutions of 0.1 mg/mL, and were corrected for buffer contribution. Secondary structure fractions were calculated from deconvolution of the CD spectra using the program K2D2 ( [31].

Determination of the biological activity: the minimum inhibitory concentration (MIC)

Minimal inhibitory concentrations (MICs) of teicoplanin and vancomycin (Sigma-Aldrich, Milan, Italy) to S. venezuelae containing pIJ86 or pIJ86ΩC-His6-vanY n or pIJ86ΩN-His6-vanY n was determined in MYM agar added with 50 μg/mL apramycin and increasing concentrations of glycopeptides. The inoculum was 106 cfu/mL (after mycelium sonication with Sonics Vibracell VCX 130 – power 130 Watt, 230 Volt, 50–60 Hertz, frequency 20 Hz 5 minutes of sonication, 20 seconds for each cycles with 90% of amplitude), and plates were incubated at 28°C until colonies appeared. MIC was the lowest concentration of the antibiotic that inhibits the visible growth of the recombinant S. venezuelae strains [32].


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We acknowledge EUFP7/2007-2011 Metaexplore grant agreement No: 222625 to GLM and FM for funding our research on novel heterologous hosts for protein expression. This work was also supported by grants from Fondo di Ateneo per la Ricerca to FM, Progetto Cariplo: Promuovere Capitale Umano d’Eccellenza to EB and GLM, and by MIUR fellowships to GLM and FB. We appreciate the support from Consorzio Interuniversitario per le Biotecnologie (CIB).

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Correspondence to Elisa Binda.

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The authors declare that they have no competing interests.

Authors’ contributions

FM conceived the project and wrote the paper. EB performed most of the experiments on protein expression, purification and biochemical characterization, and prepared figures and tables. GLM developed conjugation and molecular biology tools. FB focused on protein purification procedures. LP designed the experiments on the protein biochemistry. All authors have read and approved the final manuscript.

Electronic supplementary material

Additional file 1: Figure S1: SDS-PAGE Analysis of C-His6-VanYn and N-His6-VanYn from S. venezuelae recombinant strains as in Figure 2 main text. Analysis of samples corresponding to cellular and extracellular fractions from cultures of S. venezuelae recombinant strains grown in YEME for 72 hours. From S. venezuelae pIJ86ΩN-His6-vanY n : extracellular fraction (lane 1), soluble cell-free fraction (lane 2), insoluble cell-free fraction (lane 3) and cell wall fraction (lane 4); from S. venezuelae pIJ86ΩC-His6-vanY n : extracellular fraction (lane 5), soluble cell-free fraction (lane 6), insoluble cell-free fraction (lane 7) and cell wall fraction (lane 8). In each lane, samples corresponding to 100 μL of cell culture were loaded. Std reference protein: C-His6-VanYn from E. coli (5 μg, 25 kDa). (PDF 544 KB)

Additional file 2: Figure S2: SDS-PAGE Analysis of C-His6-VanYn from S. venezuelae recombinant strain growth in 3-L batch fermentor as in Figure 3 main text. Crude extracts of cell samples collected at different times of fermentation: 18 (lane 1), 24 (lane 2), 48 (lane 3), 72 (lane 4), 96 (lane 5), 120 (lane 6), 144 (lane 7), 168 (lane 8) hours. In each lane, samples corresponding to 100 μL of cell culture were loaded. Std reference protein: C-His6-VanYn from E. coli (5 μg, 25 kDa). (PDF 455 KB)

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Binda, E., Marcone, G.L., Berini, F. et al. Streptomyces spp. as efficient expression system for a d,d-peptidase/d,d-carboxypeptidase involved in glycopeptide antibiotic resistance. BMC Biotechnol 13, 24 (2013).

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  • Streptomyces
  • Heterologous protein production
  • d,d-carboxypeptidases
  • Glycopeptide production
  • Glycopeptide resistance
  • Dalbavancin