The O-mannosylation and production of recombinant APA (45/47 KDa) protein from Mycobacterium tuberculosis in Streptomyces lividans is affected by culture conditions in shake flasks
© Gamboa-Suasnavart et al; licensee BioMed Central Ltd. 2011
Received: 6 October 2011
Accepted: 20 December 2011
Published: 20 December 2011
The Ala-Pro-rich O-glycoprotein known as the 45/47 kDa or APA antigen from Mycobacterium tuberculosis is an immunodominant adhesin restricted to mycobacterium genus and has been proposed as an alternative candidate to generate a new vaccine against tuberculosis or for diagnosis kits. In this work, the recombinant O-glycoprotein APA was produced by the non-pathogenic filamentous bacteria Streptomyces lividans, evaluating three different culture conditions. This strain is known for its ability to produce heterologous proteins in a shorter time compared to M. tuberculosis.
Three different shake flask geometries were used to provide different shear and oxygenation conditions; and the impact of those conditions on the morphology of S. lividans and the production of rAPA was characterized and evaluated. Small unbranched free filaments and mycelial clumps were found in baffled and coiled shake flasks, but one order of magnitude larger pellets were found in conventional shake flasks. The production of rAPA is around 3 times higher in small mycelia than in larger pellets, most probably due to difficulties in mass transfer inside pellets. Moreover, there are four putative sites of O-mannosylation in native APA, one of which is located at the carboxy-terminal region. The carbohydrate composition of this site was determined for rAPA by mass spectrometry analysis, and was found to contain different glycoforms depending on culture conditions. Up to two mannoses residues were found in cultures carried out in conventional shake flasks, and up to five mannoses residues were determined in coiled and baffled shake flasks.
The shear and/or oxygenation parameters determine the bacterial morphology, the productivity, and the O-mannosylation of rAPA in S. lividans. As demonstrated here, culture conditions have to be carefully controlled in order to obtain recombinant O-glycosylated proteins with similar "quality" in bacteria, particularly, if the protein activity depends on the glycosylation pattern. Furthermore, it will be an interesting exercise to determine the effect of shear and oxygen in shake flasks, to obtain evidences that may be useful in scaling-up these processes to bioreactors. Another approach will be using lab-scale bioreactors under well-controlled conditions, and study the impact of those on rAPA productivity and quality.
KeywordsShake flasks shear oxygenation APA 45/47 kDa O-mannosylation Mycobacterium tuberculosis Streptomyces lividans
Mycobacterium tuberculosis is the main bacterial pathogen causing latent infection in more than a third of the world population, and is also developing resistance to virtually every new drug used to treat tuberculosis, resulting recently in a global emergence of extensively drug-resistant tuberculosis [1–3]. At least 41 glycoproteins were identified in culture filtrates of M. tuberculosis, and most of them seem to play important roles in M. tuberculosis infection and host immune response [4–6]. Therefore, some of those glycosylated antigens are good candidates for vaccine development and improvement of diagnosis [6–9]. The first described mannosylated protein in Actinomycetes was the Ala-Pro-rich Antigen (also known as 45/47 kDa or APA protein) in M. tuberculosis, which is immunodominant [10–12]. The specific role of APA is not clearly defined; however, it is reported as an adhesin , as well as an antigen elicitor of lympho-proliferative responses and cytokine production . It is worth of note, that the T cell response induced by APA is dependent of its glycosylation status specifically of the O-mannosylation of four of their threonines . Particularly, Thr277 presents heterogeneity from none to three mannose units in native APA . In addition, none to four mannose units were found in Thr277 of the rAPA produced in S. lividans.
Strains of Streptomyces sp. are well known as good producers of extracellular recombinant proteins; these strains also have the ability to glycosylate their own proteins, as well as heterologous proteins [15–22]. Recent studies in genetics and cell biology have revealed analogies between Streptomyces sp. and Mycobacterium sp., both belonging to the phylum Actinobacteria . Moreover, S. lividans allows the production, both in shake flasks  and in bioreactor , of large amounts of glycosylated rAPA suitable for biochemical studies and immunological assays. However, no detailed study of the effect of culture conditions on the productivity and O-glycosylation of rAPA has been reported.
On the other hand, probably more than 90% of submerged cultures for microbial research purposes are performed in shake flasks [25, 26]. These studies are carried out due to their low cost, simplicity of operation and availability to do many experiments simultaneously [27, 28]. Almost all the tasks, such as screening of strains, media optimization, strain development, elucidation of metabolic pathways, investigations of process conditions, and evaluation of fundamental growth kinetics are made in these vessels . In shake flasks the momentum and heat transfer is influenced by the geometry of the rotating bulk liquid, that is the contact area between the liquid and the friction area, i.e. the flask inner wall (and indentations in baffled flasks, or the coiled stainless steel spring in flasks) . On the other hand, the mass transfer (mainly oxygen) is influenced by the wet wall exposed to the surrounding air, this is the mass exchange area . Modifications of shake flasks by the introduction of baffles and other enhancements (like stainless steel spring coils) are frequently necessary in order to provide sufficient aeration and shear stress [25, 29, 30]. In S. lividans cultures, coiled and baffled flasks are normally used [30–33], but no detailed study has been done on how the geometry of the flasks can affect recombinant protein production, and its O-glycosylation as a function of the morphology of the filamentous bacteria.
Results and Discussion
Morphological differences in cultures carried out in conventional Erlenmeyer normal (NF), baffled (BF), and coiled shake flasks (CF). Data are presented as average ± standard deviation of image analysis of at least 100 clumps, mycelia or pellets for each sample, and at least 3 samples were analyzed for each flask. Values with the same superscript (a,b or c) are not significantly different by Tukey HSD Test (p = 0.01).
2.11 ± 1.22
1.57 ± 0.41
6.15 ± 2.32
1.51 ± 0.49
0.04 ± 0.02 a
0.23 ± 0.06 b
1.01 ± 0.35 c
2.11 ± 0.67
0.02 ± 0.01 a
0.16 ± 0.05 b
0.77 ± 0.30 c
2.66 ± 0.98
On the other hand, the larger pellets obtained in conventional flasks have a more rounded shape than the smallest clumps obtained in the other geometries. Although, no porosity measurements were carried out, the pellets can be seen to be very compact, which could bear the thought of nutritional and/or diffusional limitations within them , but not critical enough to affect bacterial growth. Manteca et al.  observed that the centre of mycelium pellets can contain inactive cells, due to a rapid consumption of substrates (nutrients and/or oxygen) within the kernel of the pellets. However, Yun et al.  reported that mass transfer concerns were negligible in S. lividans growth, when pellets reach diameters around 2 mm, at least in terms of oxygen transfer [38, 46]. Moreover, in S. lividans larger pellets some diffusional limitations might affect the internalization of the inducer, thus reducing recombinant protein production , total protein production  or the mechanisms involved in post-translational modifications of recombinant proteins [37, 47].
Identification and quantification of rAPA produced in three flasks geometries
Analysis of O-mannosylation in rAPA
Theoretical peptides generated by LysC digestion of rAPA from S. lividans.
Amino acid sequence
DPEPAPPVPTTAASPPSTAA APPAPATPVAPPPPAAANTP NAQPGDPNAAPPPADPNAP PPVIAPNAPQPVRIDNPVGG FSFALPAGWVESDAAHFDYG SALLSK
AAARLGSDMGEFYMPYPGTR INQETVSLDANGVSGSASYY EVK
ALAESIRPLVAPPPAPAPAP AEPAPAPAPAGEVAPTPTTP TPQRTLPA
Data from Figure 5 demonstrate that culture conditions (simulated by three different flasks geometries) can affect the O-mannosylation of rAPA produced in S. lividans. At least two different degrees of rAPA O-mannosylation can be obtained, but both are different from that reported by Lara et al. . Putting together all the results, it can be assumed that under other culture conditions, other glycoforms might be obtained in S. lividans or in M. tuberculosis, respectively.
Those O-mannosylation particularities suggests to play an important function in antigenic roles, because changes in glycosylation patterns of rAPA, produced in different hosts, significantly affect the ability to stimulate T lymphocytes in vivo[14, 48]. It will be interesting to evaluate the different O-glycoforms produced in the same host (S. lividans), using different culture conditions (either in shake flasks or in bioreactors), and compare them with the native protein immune response.
The relationship between shear and morphology in filamentous bacteria has been widely studied. In this work, said relationship has been corroborated for S. lividans producing a recombinant glycoprotein. In addition changes in rAPA production and the degree of O-glycosylation, both related to morphology, were observed. The different conditions of shear and mass transfer provided by the three shake flask geometries resulted in changes in aggregation morphology. Although, there were significant roundness morphological differences between baffled and coiled shake flasks, but not differences in diameter, said differences were not sufficient to affect the production of rAPA and the degree of C-terminal O-mannosylation. However, the morphology of larger pellets obtained in conventional shake flasks causes a significant decrease in rAPA production and C-terminal peptide O-mannosylation.
To our knowledge, this is the first report indicating how culture conditions can affect the O-glycosylation degree in recombinant glycoproteins produced in prokaryotes. Here, a process to obtain at least two different degrees of O-mannosylation, using three different flask geometries, was described. A better understanding of how hydrodynamic forces and oxygen/nutrient transfer inside S. lividans aggregates modify the ability to O-glycosylate recombinant proteins can be useful in further production processes, with the possibility to manipulate the immunogenic properties. Then, it would be interesting to separately determine and quantify the effect of shear stress and oxygen transfer rates in shake flasks, wherein dissolved oxygen is not controlled, in order to have evidences that can be useful to scale-up the production to a bioreactor.
Microorganism and culture conditions
Wild type S. lividans 66 strain 1326  was transformed with plasmid pIJ6021MT-45 carrying the apa gene under a thiostrepton-inducible promoter, and conferring resistance to kanamycin . A master stock of 30 mL of spores in 20% glycerol was obtained, divided into aliquots, and kept at -20°C until use. To start cultures spores were pregerminated in 2XYT medium for 6 h at 37°C and 150 rpm ; the germinated spores were then washed and sufficient spores were inoculated in order to obtain an optical density of 0.025 at 600 nm (measured in a Beckman DU730 spectrophotometer). Three different shake flask geometries were tested (250 ml, filled with 50 ml of medium): Coiled Flask (CF), Baffled Flask (BF), and conventional Erlenyemer Normal Flask (NF), as is shown in Figure 1. Coiled flasks consist of conventional normal flasks with an inserted 30 cm stainless steel spring (1.3 cm diameter, 19 sw gauge) as previously described . Culture medium was Luria-Bertani's medium with kanamycin (50 μg/mL) modified by addition of 34% w/v sucrose . All cultures were carried out at 30°C and 150 rpm for 60 h, with addition of the inducer (thiostrepton 10 μg/mL) at 16 h of culture. Two flasks were removed at each kinetic data point for biomass, protein and image analysis.
Biomass was evaluated by dry weight; 10 mL of culture were filtered through a 0.45 μm pore size membrane (Millipore), and washed once with one volume of distilled water. The mycelium obtained was dried for 24 h in an oven at 55°C, then placed for 2 h in a desiccator, and weighed afterwards.
Image analysis procedures
A sample of 20 μL of culture broth was fixed using a formaline solution (10% v/v) in order to avoid the loss of the actual morphology in fresh samples. This sample was placed on a slide, and carefully covered with a cover slip. At least 100 clumps, mycelia or pellets were analyzed for each sample, and at least 3 samples were analyzed for each flask. 2D images were obtained by an image analysis system consisting of a CCD camera (Nikon Color, KP-D50) coupled to a microscope (Nikon Optiphot-2), or a CCD camera (Nikon KP-160) mounted to a stereomicroscope (Olympus SZ40), and a PC with the image analysis software (Image Pro Plus 4.1, Media Cybernetics, Silver Spring, MD) installed in it . The software reported the average diameter and the roundness to characterize the size of aggregates, as the main results. Average diameter is defined as the diameter of a perfect circle, having the same area as the object to be measured. Roundness describes the deviation of mycelial particles from a true circle. In large aggregates (from conventional shake flasks), images were first converted to monochrome and then these grayscale images were processed using a special algorithm for aggregates . One-way ANOVA for independent and samples and pair-wise comparisons using Tukey HSD (Test for Post-ANOVA) were carried out in order to assess the morphological statistical differences between shake flask geometries. Analysis were done using Excel® (2007) and the " VassarStats: Website for Statistical Computation" available on-line of Vassar College, NY-USA (http://faculty.vassar.edu/lowry/anova1u.html).
Purification of rAPA
All cultures were centrifuged at 10,000 × g and the supernatant was filtered through a 0.45 μm membrane (Millipore). Ammonium sulfate was added to the culture filtrate to 75% saturation and the precipitated proteins were recovered by centrifugation, suspended in PBS (Phosphate Buffered Saline; 10 mM Na2HPO4, 2 mM KH2PO4) buffer, dialyzed against distilled water overnight, subsequently against an acetate buffer (Acetic acid 0.2 M, Sodium acetate 0.2 mM, pH 5.0) for 24 h, and finally against ConA binding buffer (Sodium acetate 0.1 M, NaCl 1.0 M, Mn2-4H2O 1 mM, Sodium Azide 0.01% and CaCl2-2 H2O 1 mM) for 24 h. The ConA-binding protein (47-kDa protein) was separated by affinity chromatography on ConA-Sepharose column (Concanavalin A from Canavalia ensiformis, Sigma-Aldrich), and eluted with the ConA binding buffer with α methyl-mannopyranoside 0.05 M.
Protein identification and quantification
Total protein was determined using the Thermo Scientific Pierce BCA Protein Assay Kit (Thermo-Pierce) from supernatant. Electrophoresis in 10% polyacrylamide gels containing SDS and subsequent immunoblotting procedures were carried out as previously described . For Western blots, 100 μg of total protein in SDS-PAGE (10%) were transferred to polyvinylidine difluoride membranes (Millipore). Nonspecific binding was blocked with 5% (w/v) skim milk in PBS containing Tween 20 (0.05% v/v) for one hour. After that, membranes were washed with PBS Tween 0.05%. The primary antibody mAb6A3 was added in dilution 1:500 and incubated overnight at 4°C . After three washes with PBS-Tween 20, the membranes were incubated with diluted peroxidase-conjugated anti-mouse IgG 1:1000 (Sigma-Aldrich). After incubation, the blots were stained for peroxidase activity by adding 3,3-diaminobenzidine (Sigma-Aldrich) and hydrogen peroxide (Sigma-Aldrich) in PBS and washed with tap water.
The 45 and 47 kDa bands were excised and washed with water, distained with ammonium bicarbonate buffer (100 mM) with 50% methanol, dehydrated with acetonitrile (100%), and rehydrated with ammonium bicarbonate buffer (25 mM) containing enzyme Lys-C (Roche) in dilution 1:1000. Digests were incubated overnight at 37°C, 20 μL of Trifluoroacetic acid (TFA, 0.1%) were added to stop the reaction, and concentrated in a SpeedVac concentrator (Savant-Thermo) down to a volume of 20 μL.
Masses were determined in a Bruker Microflex matrix-assisted laser desorption ionization time-of-flight instrument (Bruker Daltonics GmbH, Leipzig, Germany) equipped with a 20-Hz nitrogen laser at l = 337 nm. Spectra were recorded in reflector and/or linear positive mode for the mass range of 3800 - 6000 Da. 1.0 mL of sample solution was mixed with 5 mL of 30% Acetonitrile, 70% Water, 0.1% TFA, and saturated with a-cyano-4-hydroxycinnamic acid or sinapinic acid. Then, 1.0 μL of this solution was deposited onto the MALDI target and allowed to dry at room temperature. At least three MALDI-TOF analyses were done at the end of each independent culture.
This work was partially financed by CONACyT grants 2533, 103214, 103393, and 104951-Z, CONACYT-INNOVAPYME 137854, and PAPIIT-UNAM IN-228509-3. RGS thanks the scholarship from CONACyT (316929). Authors thank Celia Flores, M. Sc. and Enrique Galindo, PhD. (Instituto de Biotecnología, UNAM), and Marisol Córdova, PhD. (Centro de Ciencias Aplicadas y Desarrollo Tecnológico, UNAM) for their technical assistance in image analysis. Authors thank Erendida Garcia, Chem. (Instituto de Química, UNAM) for MALDI-TOF analysis. Also, Authors thank Cristina Parada M.Sc. (Instituto de Investigaciones Biomédicas, UNAM) and Prof. J. Büchs group (RWTH Aachen University) for technical assistance on protein purification and quantification. We also thank Ana Delgado for reviewing the English version of the manuscript.
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