Evaluation of scFv protein recovery from E. coli by in vitro refolding and mild solubilization process
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The production of therapeutically active single chain variable fragment (scFv) antibody is still challenging in E. coli due to the aggregation propensity of recombinant protein into inclusion bodies (IBs). However, recent advancement of biotechnology has shown substantial recovery of bioactive protein from such insoluble IBs by solubilization and refolding processes. In addition, gene fusion technology has also widely been used to improve the soluble protein production using E. coli. This study demonstrates that mild-solubilization and in vitro refolding strategies, both are capable to recover soluble scFv protein from bacterial IBs, although the degree of success is greatly influenced by different fusion tags with the target protein.
It was observed that the most commonly used fusion tag, i.e., maltose binding protein (MBP) was not only influenced the cytoplasmic expression in E. coli but also greatly improved the in vitro refolding yield of scFv protein. On the other hand, mild solubilization process potentially could recover soluble and functional scFv protein from non-classical IBs without assistance of any fusion tag and in vitro refolding step. The recovery yield achieved by mild solubilization process was also found higher than denaturation–refolding method except while scFv was refolded in fusion with MBP tag. Concomitantly, it was also observed that the soluble protein achieved by mild solubilization process was better structured and functionally more active than the one achieved by in vitro refolding method in the absence of MBP tag or refolding enhancer.
Maltose binding protein tagged scFv has shown better refolding and solubility yields as compare to mild solubilization process. However, in terms of cost, time and tag free nature, mild solubilization method for scFv recovery from bacterial IBs is considerable for therapeutic application and further structural studies.
KeywordsSingle chain variable fragment Inclusion bodies Refolding Mild solubilization Bacterial protein production
In the recent time, antibody based biomolecules are being frequently used in disease diagnosis and prevention. One of such widely used biomolecules is single chain variable fragment (scFv) antibody which is particularly attractive due to its smaller size, low immunogenicity and low cost production . However, production of fully functional scFv antibody protein from bacteria is still challenging due to its misfolding and formation of inclusion bodies (IBs) [2, 3]. Excess production of recombinant protein in the bacterial cytosol often triggers the partially folded proteins to interact with each other that results in protein aggregation thus IB formation [4, 5]. The reducing environment of the bacterial cytoplasm also contributes to protein misfolding as well as IB formation by inhibiting intra-disulfide bond formation . Generally, IBs are protein aggregates with very little or no biological activity . Currently, with the aid of recombinant technology and protein engineering, several strategies such as gene fusion technology, co-production of chaperones and foldases, use of mutated host strains, lowering expression temperatures and inducer concentration have been exploited for efficient soluble protein production in E. coli [8, 9]. Now a days, denaturation and refolding of classical and non-classical IBs are becoming prevalent to recover soluble and active protein from E. coli [10, 11, 12]. In this study, gene fusion technology was applied along with denaturation–refolding process to recover soluble scFv protein from bacterial IBs. In addition, mild solubilization strategies have been verified as high yielding and cost effective in comparison to the complete denaturation and in vitro refolding technique . To obtain bioactive protein, IBs are usually denatured with high concentration of chaotropes such as urea or guanidine hydrochloride (GdnHCl) . Sometimes, β-mercaptoethanol and dithiothreitol (DTT) are also added for proteins with multiple cysteine residues to reduce incorrect disulfide bonds . High concentration of chaotropic agent results in complete denaturation of insoluble IBs which are further subjected to a single refolding step to recover soluble protein . Alternatively, soluble protein can also be recovered directly from non-classical IBs by using non-denaturing solubilizing agents such as N-lauroyl sarcosine, dimethylsulfoxide (DMSO) and low percentage (~ 5%) of n-propanol [7, 17, 18]. Several studies have mentioned earlier that the recovery yield of soluble protein from bacterial IBs depends on its nature and the strength of denaturing agents which are applied during the solubilization process [7, 19].
Generally, in vitro refolding technology includes complete denaturation of classical IBs with high concentration of denaturing agents followed by dilution in refolding buffer and subsequent dialysis to remove excess salts and other denaturing agents [2, 20, 21]. The major drawbacks of this method are its complex and expensive operational process which further needs extensive optimization at a number of steps . In addition, use of high concentration of denaturing agent results in complete denaturation of secondary structure of IB protein leading to re-aggregation during successive refolding process . Consequently, recovery yield of soluble protein is greatly reduced during the process of in vitro refolding. Currently, with the knowledge of genetic and protein engineering, novel tailored-made strategies have been applied to improve the soluble protein production from E. coli. Gene fusion is one such commonly used technology that has shown to improve the soluble protein production in bacteria . A widely accepted study has shown that fusion of maltose binding protein (MBP) at the C-terminal of recombinant scFv greatly influences its soluble and functional expression in E. coli [25, 26]. Another recent study has shown that MBP-scFv conjugates retain better in vitro solubility and stability as compared to untagged scFv . The current study has also shown that MBP tag not only influences the cytoplasmic expression of E. coli, but also greatly improves the in vitro refolding yield of scFv protein. On the other hand, the mild solubilization process using high pH buffers, high pressure, detergents, organic solvents and low concentration of chaotropes help to retain native secondary structure of the protein [23, 27, 28, 29, 30].
Construction of scFv antibody
Generally, scFv antibody is constructed with variable heavy (VH) and variable light (VL) chain by covalently linking with a short peptide that is mostly composed of Glycine, Serine and Alanine residues . Herein, the amino acid sequences of all the six CDRs of variable heavy chain (VH) and variable light chain (VL) were assembled from an anti-fusion loop dengue E53 Fab antibody (PDB: 3IXY) by joining with 15 amino acid (Gly4Ser)3 long linker to create a full length scFv antibody protein molecule . The structural integrity of newly designed scFv molecule was verified by in silico homology modelling and superimposition on parental E53 Fab molecule (Additional file 1: Figure S1). After codon optimization for P. pastoris and E. coli, the newly designed scFv gene was de novo synthesized from GeneArt (Invitrogen™).
Cloning of scFv antibody gene
The scFv insert gene was restriction digested from recombinant pJET1.2 cloning vector and was further used for recombination in pET28a(+), pGEX-4T-1 and pMAL-p5X expression vector. The resulting recombinant plasmids, i.e., scFv-pET28a(+), His.scFv-pET28a(+), GST.scFv-pGEX-4T-1 and MBP.scFv-pMAL-p5X (Additional file 2: Figure S2, Additional file 3: Figure S3) were further subjected to restriction digestion with the corresponding set of restriction enzymes in order to confirm the proper ligation. In agarose gel electrophoresis, all of the recombinants showed fall out at around 700 bp DNA ladder that confirmed proper integration of the desire scFv insert of 732 bp length in the target expression vector.
Expression of scFv antibody protein
ScFv antibody proteins without any tag and with different fusion tags such as 6xHis, GST and MBP, were expressed in E. coli in different growth condition. In normal expression condition, none of the verified scFvs, neither with 6xHis, GST and MBP tags nor without any tag were expressed in soluble form. The scFv expression in E. coli was also analyzed by lowering expression temperature and inducer concentrations. Unfortunately, the scFv expression in soluble fraction was remaining almost unchanged as it was in E. coli under normal expression condition (Additional file 4: Figure S4). However, due to the reducing condition of E. coli cytoplasm, expressed scFvs are hardly capable to form disulfide bonds, hence mostly renders in insoluble aggregation as IBs [25, 33, 34]. The most common solution for that is secretion of the scFv to the bacterial periplasm where the oxidizing condition facilitates the disulfide bonds formation . It has already been reported that scFv in fusion with MBP, efficiently expresses in bacterial periplasm as a soluble and active form . In addition, MBP is a stable monomer and does not induce artificial dimerization or aggregation . Here, a significant level of scFv expression in soluble fraction was also observed (Additional file 5: Figure S5) while scFv was expressed in fusion with MBP tag and was extracted following periplasm specific protocol. Several biochemical and biophysical studies have revealed that MBP carries large hydrophobic cleft exposed on its surface where fused polypeptide interacts with fusion partner rendering it inaccessible to form aggregation [36, 37]. Moreover, MBP have certain structural flexibility regarding to the hydrophobic cleft on its surface where different polypeptide can accommodate easily and block self-association during folding process.
Mild-solubilization, denaturation and refolding of scFv inclusion bodies
On the other hand, the recombinant scFv (without any tag) was also expressed in E. coli 500 mL LB culture at normal bacterial growth condition. Generally, in normal growth condition, major fraction of recombinant protein expresses in the form of non-classical IBs. Therefore, the resulting IBs were solubilized with mild denaturing agents such as 2 M urea, 5% DMSO, 5% isopropanol, 4 M GSSG in 50 mM PBS (pH 7.4). After high-speed centrifugation (greater than 20,000g for 10 min), the resulting supernatant was separated on 12% SDS polyacrylamide gel. Surprisingly, an intense band around 25 kDa protein marker was visualized in gel after staining with coomassie brilliant blue (Fig. 1a). The possible reason of increasing such prompt solubility yield comes from the fact that the mild solubilizing agent would not allow complete denaturation of protein, and might retain some extent of the existing secondary structure. Therefore, during re-naturation pathway, this partially folded protein does not allow more aggregation as like completely denatured protein that finally leads to improve the recovery yield of soluble scFv protein.
Comparative analysis of solubility, refolding and overall pure scFv recovery yields achieved by mild-solubilization and in vitro refolding process
Soluble and pure scFv protein yields recovered by mild solubilization and in vitro refolding methods
Solublilized IB protein (mg)
Solubility and refolding yield (mg)
Solubility and refolding yield (%)
Soluble and pure protein yield (mg)
Recovery yield of pure scFv (%)
42.67 ± 6.0
19.84 ± 4.8
46.09 ± 4.3
12.3 ± 2.7
29.15 ± 1.8
65.33 ± 5.1
7.24 ± 1.3
11.08 ± 1.7
4.73 ± 0.5
7.26 ± 0.6
72.0 ± 4.2
5.13 ± 0.8
7.12 ± 0.7
1.18 ± 0.4
1.67 ± 0.65
35.33 ± 5.4
17.42 ± 3.7
49.3 ± 4.8
15.59 × 3.4
44.13 ± 4.7
On the other hand, approximately 30% of pure scFv protein (without any tag) was recovered from insoluble IB pellet of E. coli by applying mild solubilizing method. However, in case of denaturation and refolding method, scFv with MBP tag was found to be the best in terms of recovery yield (~ 44%) whereas scFv in fusion with 6xHis and GST tag were identified as poor recovery potential around 7.2% and 1.6% respectively from insoluble IB pellet of E. coli (Table 1, Additional file 6: Figure S6). These findings are also symmetrical with our earlier remark that MBP enhances refolding yield by promoting solubility, and due to the aggregation propensity of GST tag, GST-scFv shows poor solubility  and refolding yield whereas, scFv with 6xHis tag showed little refolding potential as it has neither solubility capacity nor excess aggregation inclination . Therefore, it can be inferred that without presence of solubility enhancing tag, scFv cannot refold properly in extra cellular condition.
Structural analysis of soluble scFv protein
Binding analysis of soluble scFv proteins by ELISA
To study the binding activity of soluble scFv protein recovered by mild solubilization and denaturing–refolding method, direct ELISA and SPR analysis were performed. Here, the recombinant FuBC loop of dengue envelope protein has been used as bait since the amino acid sequences of VH and VL chains of our currently developed scFv molecule were taken from the anti-fusion loop of dengue E53 Fab antibody (PDB: 3IXY). It can also be noted here that Fu and BC are two highly conserved loop of dengue envelope domain II, were fused together to construct an ORF for the development of recombinant FuBC protein (Rathore et al. unpublished work). On the other hand, soluble scFvs achieved by mild solubilization (without any tag) and denaturation–refolding (with 6xHis, GST and MBP tags) methods were biotinylated and the binding was measured in direct ELISA by using them as primary antibody. Along with each set of experimental titer, one set of control titer was always used without applying any biotinylated scFv. The reading of multiple ELISA titers suggests that scFv with MBP fusion tag binds with dengue FuBC loop in higher intensity in compare to scFv with 6xHis and GST fusion tags. However, it should be noted that the signal achieved by MBP-scFv conjugate was not only developed by scFv alone but also mostly contributed by MBP tag as it shares 60% MW of total MBP-scFv fusion protein. On the other hand, soluble scFv recovered by mild solubilization method showed relatively higher titer value without assistance of any fusion tag (Fig. 4). It might be due to the result of using mild denaturing agent that does not denature protein completely, retains some extent of secondary structure, and showed better structural and functional integrity.
Binding analysis of soluble scFv proteins by SPR assay
Apparently, it is plausible that the in vitro refolding method in fusion with MBP tag is more effective for scFv recovery compare to mild solubilization process. However, scFv expressed in fusion with 6xHis and GST tags revealed poor recovery yield. Therefore, it is easily acceptable that scFv alone cannot refold properly and the yield achieved by in vitro refolding in fusion with MBP was due to solubility enhancing property of MBP. However, it is necessary to remove the fusion tag from final protein as it potentially interferes with proper structure and function of the target protein [45, 46]. Therefore, after removal of fusion tag, the final yield will at least be 60% less than of current recovery yield as the MBP (43 kDa) tag contributes more than 60% MW of the complete MBP-scFv (70.3 kDa) conjugate. In addition, several studies have also reported previously that tag removal is not only a time consuming expensive process but also greatly hinder overall recovery yield by acceleration of re-aggregation [43, 45]. On the other hand, mild solubilization process have shown around 30% overall scFv pure protein recovery yield without assistance of any solubility enhancing tag. It was also described previously that mild solubilization method uses non-classical IBs and low concentration of denaturing agents as it preserves native-like secondary structures during recovery process. Therefore, mild solubilization method is better for further functional and structural study or therapeutic applications with any recombinant protein as it is always preferred to work with protein comprising native conformation. In addition, mild solubilization would not require any refolding and tag removal process, as it would save extra-time, cost and potentially would avoid re-aggregation thus final recovery yield will be unchanged.
Formation of IBs is the major challenge for large-scale recovery of bioactive protein from E. coli. Several gene fusions and refolding technology have been employed to improve the recovery yield of recombinant protein from bacterial IBs. Despite being widely utilized to improve soluble protein production in E. coli, fusion tags and refolding technology are still not well accepted due to non-native low yield protein recovery and re-aggregation propensity after removal of fusion tags. Therefore, the mild solubilization method could be utilized to recover bioactive protein from such insoluble IBs that provide a notable alternative to the conventional use of fusion tags (e.g., 6xHis, GST and MBP) and in vitro refolding process. The recovery yield achieved by the denaturation–refolding method was better than that achieved by the mild solubilization process while scFv was expressed and refolded infusion with MBP tag. Since, it is necessary to remove the tags before performing functional and structural analyses or any therapeutic applications as removing of MBP tag from MBP-scFv conjugates would decrease the overall yield by 60%, because MBP contributes more than 60% molecular weight of total MBP-scFv fusion protein. Hence, it can be concluded that both of the mild-solubilization and in vitro refolding strategies are capable to recover soluble scFv protein from bacterial IBs, however due to tag free nature and retaining native secondary conformation, the mild solubilization is comparatively better for recombinant protein production. Since it was observed that the soluble scFv protein recovered by the mild-solubilization process could retain proper structure and function without assistance of any fusion tag, it could be a better choice for efficient and economical recombinant protein production in E. coli. Further optimization of mild-solubilization method might result in the high-throughput recovery of therapeutic proteins from bacterial inclusion bodies.
Materials and methods
Chemicals and reagents
The principal components of bacterial culture: Luria–Bertani broth, tryptone and yeast extract; antibiotics: ampicillin, kanamycin; protein expression and analysis reagents: isopropyl β-d-1-thiogalactopyranoside (IPTG), Tris HCL and base, Glycine, lysozyme, phenylmethylsulfonyl fluoride (PMSF), sodium dodecyl sulphate (SDS), acrylamide/bis-acrylamide, ammonium persulfate (APS), tetramethylethylenediamine (TEMED), dithiothreitol (DTT), and ethylene-di-aminetetraacetic acid (EDTA), coomassie G-250 were purchased from Himedia and VWR life science. Inclusion body (IB) solubilizing and protein refolding reagents: guanidine hydrochloride (GdnHCl), urea, arginine hydrochloride (ArgHCl), isopropanol were from Sigma-Aldrich. PCR cloning kit: pJET1.2; all restriction enzymes; T4 DNA ligase and rapid protein assay BCA kit were from New England Biolabs (NEB) and Thermo Scientific. ELISA reagents: bovine serum albumin (BSA), Tween-20, Citric acid, H2O2, o-phenylenediamine dihydrochloride (OPD) were from Sigma-Aldrich and Alfa Aesar. Protein purification apparatus superose 12 10/300 size exclusion column was purchased from GE Healthcare. Affinity measuring Biacore T200 instrument and structure figuring Circular Dichroism (CD) Spectrometer facilities were provided by AIRF, Jawaharlal Nehru University, New Delhi-110021, India.
Construction and synthesis of scFv antibody gene
The amino acid sequences of all the six CDRs of variable heavy chain (VH) and variable light chain (VL) of an anti-fusion loop dengue E53 Fab antibody (PDB: 3IXY) were joined by 15 amino acids (Gly4Ser)3 long linker to create a full length scFv antibody protein molecule. The structural integrity of the newly designed scFv molecule was verified by in silico homology modeling, and by superimposing on the parental E53 Fab molecule. After that, the corresponding scFv gene of the newly designed scFv antibody protein was de novo synthesized from GeneArt (Invitrogen™).
Designing and cloning of scFv gene with and without fusion tag
Primarily, the synthetic scFv gene was PCR amplified with three pairs of primers (Additional file 7) that were flanked by three different sets of restriction sites. The PCR products of scFv were then recombined in the pJET1.2 PCR cloning vector, and digested with specific set of restriction enzymes to prepare targeted scFv inserts. The resulting scFv inserts were then eluted from the agarose gel and finally, sub-cloned into the pET28a(+) vector under the control of T7 promoter using NcoI and EcoRI restriction sites excluding N-terminal 6xHis tag sequence, and also in between EcoRI and XhoI restriction sites including 6xHis tag sequence at N-terminus (Additional file 2: Figure S2). Additionally, the scFv insert was also sub-cloned in pGEX-4T-1 vector using EcoRI and XhoI restriction sites, and in pMAL-p5X vector using NdeI and EcoRI restriction sites that included GST and MBP tags respectively at N terminus (Additional file 3: Figure S3). The recombinant constructs were further verified by Sanger sequencing.
Expression and extraction of scFv recombinant protein
Escherichia coli BL21 (DE3) cells were transformed with the four recombinant vectors, namely scFv-pET28a(+), His.scFv-pET28a(+), GST.scFv-pGEX-4T-1 and MBP.scFv-pMAL-p5X that encloses only scFv gene (without any tags) and also scFv with 6xHis, GST and MBP tags respectively. The transformed cells were grown overnight in LB agar plates in presence of ampicillin for scFv-pET28a(+) and His.scFv-pET28a(+) clone and in presence of kanamycin for GST.scFv-pGEX-4T-1 and MBP.scFv-pMAL-p5X clone at 37 °C temperature. Single colony from each plate was then inoculated in four different LB broths with 100 µg/mL ampicillin or 50 µg/mL of kanamycin. The primary cultures grown overnight were re-inoculated in fresh LB broth with corresponding antibiotic, and followed to grown up at 37 °C till OD600 reached 0.5. All of the secondary cultures grown at 37 °C were then split into three groups, first group was induced with IPTG 1.0 mM concentration and grown at 37 °C for 4 h, second group was induced with 0.5 mM IPTG concentration and grown at 30 °C for 4 h and the third group was induced at 0.5 mM IPTG concentration but grown at 20 °C for overnight. The cells were then harvested by centrifugation at 4000g and the cell pellets were re-suspended with lysis buffer containing 50 mM Tris–HCl pH 8.0, 1 mM CaCl2, with 0.5% triton X-100, lysozyme 1.0 mg/mL, 1 mM EDTA and 1 mM PMSF. Cell lysates were kept on rocker for an hour at room temperature and then centrifuged at 12,000g. The crude supernatant was collected for all clonal expression, and the pellets were re-suspended with equal volume of lysis buffer without any lysozyme. Finally, scFv expression level in all supernatants and pellets were separated on SDS-PAGE.
Escherichia coli expression and preparation of scFv inclusion bodies
The primary cultures of all scFv recombinant clones such as scFv-pET28a(+), His.scFv-pET28a(+), GST.scFv-pGEX-4T-1 and MBP.scFv-pMAL-p5X were used for inoculation of 0.5 L super-broth (10 g yeast extract, 16 g tryptone and 2.5 g NaCl) supplemented with 1 mM antibiotic, 4% MgSO4, and 20% sucrose. The secondary cultures were grown for 2–3 h at 37 °C up to OD600 0.5, and to induce recombinant protein expression 1 mM IPTG was added. Subsequently, the cultures were incubated again for another 4 to 5 h at 37 °C, and the cells were harvested with centrifugation at 4000g for 20 min. Accordingly, the harvested cell pellets were re-suspended thoroughly in 60 mL TE 50/20 (Tris pH 8.0 50 mM and EDTA 20 mM) buffer and 0.5 mg/mL lysozyme, and cell suspensions were kept on rocker for 60 min at room temperature with periodic vigorous mixing. 10 mL of 5 M NaCl, 25% triton X-100 were added, and kept on rocker for another 30 min to stop the lysis reaction. Volume was made up to 100 mL with TE 50/20 buffer, and the lysed solution were allowed for sonication at 50% amplitude, 5 s on/off pulse with 1 min gap interval until sample thinned. After that, centrifugation was performed at 10,000g for 20 min at 4 °C, supernatant was removed, and the pellets were re-suspended with 50 mL TE 50/20 and 1% triton X-100. Similarly as before, four more times triton X-100 free sonication followed by centrifugation of re-suspended pellets was carried out to retrieve clean IBs. Before last centrifugation, two aliquots of 100 µL from total 100 mL of lysate were kept aside and later centrifuged separately at 14,000g for 5 min to check IB protein concentration and banding pattern on SDS-PAGE.
Denaturation and mild-solubilization of scFv inclusion bodies
The pellets of scFv inclusion body prep retrieved from His.scFv-pET28a(+), GST.scFv-pGEX-4T-1 and MBP.scFv-pMAL-p5X clone were denatured thoroughly with 6 M GdnHCl, 100 mM Tris pH 8.1 buffer and 10 mM DTT at greater than 5 mg/mL approximate protein concentration (measured by BCA protein assay kit) which were then kept 2 h on rocker for gentle rotation. The dissolved proteins were then centrifuged at 25,000g for 20 min, and the supernatants were collected in 15 mL conical tubes for further refolding experiment. On the other hand, the non-classical IBs of tag free scFv-pET28a(+) clone was retrieved from E. coli, and was solubilized with mild denaturing agents such as 100 mM Tris pH 8.1, 2 M urea, 5% DMSO, 5% n-propanol and 4 mM oxidized glutathione; which was then allowed for overnight incubation at 4 °C temperature in gentle rotation. Finally, centrifugation was carried out at 20,000g for 20 min and the collected supernatant was checked on SDS-PAGE. The verified supernatant was further allowed for direct purification by size exclusion chromatography.
Refolding and dialysis of solubilized scFv inclusion bodies
The solubilized proteins achieved from inclusion body denaturation, were added as 50 µg/mL concentrations in chilled buffer containing 4.5 M urea, 550 mM l-arginine HCl, 100 mM Tris–HCl pH 8.1, 1 mM of reduced glutathione (GSH), 0.1 mM of oxidized glutathione (GSSG), and were allowed for refolding reaction at 4 °C for 48 h. To remove excess urea and salts, the refolding protein solutions were transferred in membrane tube (10 kD MWCO), and were allowed for serial dialysis, first day in 2 L water for 200 mL refolding mixture in cold room (4 °C) followed by another 3 days in 2 L 10 mM Tris pH 8.1 buffer getting up to 10,000 times dilution. After 4 days, the diluted protein samples were concentrated by using Millipore-Amicon 15 mL filter (10 kD MWCO) up to concentration 0.1–1.0 mg/mL.
Purification of soluble scFv antibody protein
The concentrated soluble scFv proteins either recovered by mild solubilization or denaturation–refolding methods were further allowed for FPLC (size exclusion chromatography) purification by using superose 12 10/300 column. The column was pre-equilibrated with PBS (50 mM phosphate buffer pH 7.4 and 150 mM NaCl), and the protein sample was also eluted with same PBS buffer. One mL protein sample was injected in each run by using 1 mL loop at 0.8 mL/min flow rate. The elution profile of the injected protein was monitored by UV absorbance at 280 nm on AKTA FPLC system with U9-L UV monitor. All of the peaks greater than 10 mAU were collected separately by using FPLC fraction collector, and further concentrated using 0.5 mL Millipore-Amicon filter. Pierce™ BCA protein assay kit (Pierce, USA) was used to determine the protein concentration of solubilized, refolded and purified form. All the protein samples were separated on 12% SDS-PAGE gel, and visualized by staining with coomassie-blue. Specific scFv bands were analyzed by comparing with pre-stained protein marker (PageRuler™).
Structural analysis by CD spectroscopy
To study the structural integrity of scFv protein, the scFv proteins either achieved by mild-solubilized or in vitro refolding were characterized by CD spectroscopy. 400 µL of each scFv protein samples at 0.1 mg/mL concentration (diluted in buffer 10 mM Tris–HCl, pH 8.1) was taken in 1 mm cuvette for recording far UV spectra from 200 nm to 280 nm with step size of 1 nm to bandwidth 1 nm. The measurement was performed at room temperature (22 °C), and the UV spectra were recorded for each sample with five scan. Additionally, the CD spectra for each sample were presented by taking average of two independent measurements, each averaged of five scans.
Binding analysis by direct ELISA
Binding analysis of mild-solubilized and refolded scFv antibody proteins was done by direct ELISA using 96 well flat bottom polystyrene plates. The recombinant FuBC loop of dengue envelope protein was coated on the ELISA plate, and biotinylated scFv without and with different tags were used as primary antibody followed by streptavidin–horseradish peroxidase conjugate as secondary antibody. Initially, the recombinant FuBC protein at 2 µg/mL concentration was diluted in 100 µL of 50 mM sodium carbonate buffer pH 9.5, and was coated into each well of 96-well ELISA plate for overnight. The unbound protein sample was washed with PBST buffer (PBS with 0.05% Tween 20), and the untenanted space was blocked with 2.5% (w/v) Bovine serum albumin (BSA) dissolved in PBS. To appraise the reaction rate, 100 µL of each biotinylated scFv without and with different tags were applied at different concentrations ranging from 5 µM to 300 nM and was incubated for 1 h at room temperature. Biotinylation of each scFvs was performed by using Thermo Scientific EZ-Link Sulfo-NHS-LC-Biotinylation Kit (Pierce High sensitivity Streptavidin-HRP), and by following the amine coupling protocol. Excess biotin was removed by using Zeba™ spin desalting columns after performing amine-coupling reaction. The unbound biotinylated scFvs during ELISA were washed with PBST buffer, and remaining plate was incubated with anti-goat HRP conjugated antibody diluted in PBS at 1:5000 ratios. After 30 min incubation at room temperature, the plate was washed three times with PBST, and later the direct ELISA signal was developed using O-phenylenediamine (OPD) substrate solution that was prepared in 100 mM sodium citrate buffer pH 5.0 with 0.003% H2O2. After 5 min of OPD substrate addition, 50 µL of 2 M H2SO4 was added to stop the colorimetric reaction. The intensity of developed color by the reactions were measured by using Biotek Synergy HT micro plate ELISA reader at 492 nm absorbance. It can be noted here that scFv was designed targeting FuBC loop of dengue envelope protein as its VH and VL domain sequences were driven from an anti-fusion loop dengue E53 Fab antibody (PDB: 3IXY).
Validation of scFv binding by SPR assay
To validate the binding activity of scFvs either recovered by mild solubilization or by in vitro refolding were allowed for SPR interaction experiment on a Biacore T200 instrument (GE Healthcare). Recombinant FuBC protein was immobilized on gold plate of SPR device. For binding of FuBC protein sample on the surface of the gold disc, amine-coupling reaction was carried out. 1-Ethyl-3-(3-dimethylaminopropyl) carbodiimide (EDAC) and N-hydroxysuccinimide (NHS) were used for activation of the disc for coupling reaction. NHS activates the carboxymethyl groups by creating a highly reactive succinimide ester on disc surface, which reacts with amine, and other nucleophilic groups on proteins that subsequently helps binding of target protein. Ethanolamine was added to block the remaining activated carboxymethyl group. Then, all of the analytic scFv proteins at 100 µM concentration were injected in experimental flow cells, as well as a non-specific protein sample was injected in control flow cells to obtain its relative binding profile. In all of the SPR experiments, non-specific binding obtained in the control flow cell was subtracted from the refractive signal obtained in the experimental flow cell. For qualitative binding analysis, all of the scFvs (100 µM diluted in running buffer) were injected at a flow rate 20 µL/min over 2 min. In between injections, the surface of the sensor chip was regenerated by injecting 2 M NaCl for 15 s at the same flow rate. The bulk signal caused by refractive index differences between the flow buffer and the buffer containing the analytes were systematically excluded from the data-fitting process. Moreover, for FuBC surface coupling reaction, 150 mM NaCl, 3 mM EDTA, 0.005% surfactant P20, and 10 mM HEPES–NaOH, pH 7.4, were used, and 50 mM phosphate, 150 mM NaCl pH 7.1 was used as running buffer.
AS and RDG hypothesized the objectives. AS and ASR performed the experiments. AS and RDG analyzed the data and wrote the manuscript. All authors read and approved the final manuscript.
ASR thanks University Grants Commission (UGC), India for Senior Research Fellowship. AS and RDG thanks South Asian University for financial support.
The authors declare that they have no competing interests.
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