A chicken bioreactor for efficient production of functional cytokines
The global market for protein drugs has the highest compound annual growth rate of any pharmaceutical class but their availability, especially outside of the US market, is compromised by the high cost of manufacture and validation compared to traditional chemical drugs. Improvements in transgenic technologies allow valuable proteins to be produced by genetically-modified animals; several therapeutic proteins from such animal bioreactors are already on the market after successful clinical trials and regulatory approval. Chickens have lagged behind mammals in bioreactor development, despite a number of potential advantages, due to the historic difficulty in producing transgenic birds, but the production of therapeutic proteins in egg white of transgenic chickens would substantially lower costs across the entire production cycle compared to traditional cell culture-based production systems. This could lead to more affordable treatments and wider markets, including in developing countries and for animal health applications.
Here we report the efficient generation of new transgenic chicken lines to optimize protein production in eggs. As proof-of-concept, we describe the expression, purification and functional characterization of three pharmaceutical proteins, the human cytokine interferon α2a and two species-specific Fc fusions of the cytokine CSF1.
Our work optimizes and validates a transgenic chicken system for the cost-effective production of pure, high quality, biologically active protein for therapeutics and other applications.
KeywordsTransgenic animals Biologics Recombinant proteins Cytokines Animal biotechnology
Colony stimulating factor 1
Equine infectious anemia virus
Estrogen-responsive enhancer element
Granulocyte colony stimulating factor
Granulocyte-macrophage colony stimulating factor
Good manufacturing process
Interferon-stimulated response element
Lysozyme signal peptide
Long terminal repeats
Optimized woodchuck hepatitis virus posttranscriptional regulatory element
Steroid-dependent regulatory element
Size exclusion chromatography
Since the development of recombinant human insulin, protein-based therapeutics have been the fastest-growing segment of the pharmaceutical industry. Three of the five highest revenue drugs in oncology, Rituxan, Avastin and Herceptin, are monoclonal antibodies . The appearance of hundreds of non-antibody therapeutic proteins, including enzymes, cytokines and growth factors and blood proteins, validates predictions from 2004  that this would be an area of significant growth. Between 2011 and 2016, 62 new therapeutic protein drugs were approved by the US FDA . A further 27 were approved between September 2016 and December 2017 . Although the unique benefits of biopharmaceuticals are clear, the costs to the health care system are becoming prohibitive . Prices charged have traditionally been based upon patient benefit, but the cost of goods is also significant, especially in the transition to generics and biosimilars. Many biopharmaceuticals are produced using bacterial, yeast or mammalian cell culture expression systems. Current mammalian cell-culture based systems are increasingly optimised and industrialized . Each system is constrained in some measure by yield, cost, complex purification procedures and appropriate post-translational modification when required for biological function.
Development of genetic modification systems for livestock offered the possibility of harnessing natural high-volume protein production systems (e.g. milk from farmed livestock and eggs from poultry) for the production of biologics. Transgenic sheep, goats and cows were generated that produced biopharmaceuticals in their milk, with the aim of establishing animal bioreactors for large scale production of high quality proteins, potentially at lower capital and production costs than cell culture systems [7, 8]. The first drug produced in a transgenic animal, antithrombin III in goat milk, was approved for use by the European Medicines Agency in 2006 and the FDA in 2009 . However, there are limitations to the use of large mammals as bioreactors. They have few offspring, long gestation times and require a large amount of space and feed, all of which can make industrial scale-up difficult and expensive. It can also be difficult to purify a recombinant protein from milk due to the high content of lipids and other proteins . Reabsorption of the protein by the animal can have deleterious effects, particularly if the human protein is biologically active in the host .
Interest in developing the laying hen as a bioreactor is based on the high protein synthetic capacity of the hen: an average 60 g egg contains nearly 3.5 g of protein in the egg white  and each hen may lay over 300 eggs per year. Chickens are relatively inexpensive to keep  and large flocks can be built quickly from small numbers of founder birds. In addition, chickens have closely-related glycosylation patterns to humans , which may result in reduced immunogenicity of biologics from egg white, as well as improving functionality of proteins where glycosylation is required for activity [13, 14, 15]. We showed previously that lentiviruses can be used for efficient production of transgenic chickens . Transgene expression can be restricted to the oviduct (and thus egg white) using sequences from the ovalbumin gene, encoding the most abundant egg white protein . While this approach allowed successful production of two biologically active proteins in egg white, the expression levels achieved were well below the > 1 g/L likely to be required as the basis of a commercially viable system. In addition, purification of recombinant proteins from egg white, a matrix characterized by high levels of other proteins including albumin and the gel-like glycoconjugate ovomucin, remained to be tackled . Here we demonstrate the improved and optimized production of two new proteins, including a cytokine dimer, and robust purification protocols. Interferon α2a is a legacy, off-patent biologic used to treat certain forms of cancer and hepatitis [18, 19, 20] and was selected as a model for biosimilar production in the chicken system. Macrophage colony-stimulating factor (CSF1) is a candidate therapeutic protein in many areas of regenerative medicine . Like interferon, CSF1 is a 4-helix bundle protein, structurally-related to many cytokines, including insulin, somatotrophin, placental lactogen, G-CSF, GM-CSF and erythropoietin (EPO)  that are in widespread clinical use. Immunoglobulin Fc fusion proteins are an emerging class of biopharmaceuticals [23, 24]. Several therapeutic 4 helix bundle proteins have been tested as fusion proteins with the Fc region to improve their circulating half-life and biological activity [24, 25, 26, 27, 28]. We recently produced a Fc fusion protein of CSF1 and demonstrated increased in vivo efficacy in rodent and large animal models, and potential as therapeutic in liver regeneration [29, 30, 31, 32]. An additional attraction of the Fc tag in generation of therapeutic proteins in bioreactors is that it provides a generic tag for affinity purification. Here we demonstrate the optimal production, downstream processing and biological activity of recombinant proteins produced in the transgenic avian system. The chicken bioreactor clearly has the potential to address the cost and availability of therapeutic proteins for both human and veterinary medicine.
Production of a high-purity, biologically active human cytokine
A multi-step purification protocol was developed that involves clarification of ovomucin by pH reduction and its removal by centrifugation, and purification of the interferon α2a by HiTrap Blue capture followed by size exclusion chromatography (SEC) polishing; purity was confirmed by SDS-PAGE (Fig. 1d). Recovery of interferon α2a was approximately 15 mg from 100 mL of egg white, which is 60% of the original 25 mg/100 mL estimate determined by ELISA, with most of the loss occurring in the wash of the capture step; there is no observable protein loss in the ovomucin precipitation step or polishing step (Fig. 1e). Purity of > 95% was determined by reversed phase chromatography and SEC-multi-angle light scattering analyzes (Additional file 2: Figure S2).
The anti-viral properties of the purified interferon α2a were examined using a dose-inhibition assay against an H1N1 influenza A virus (A/Puerto Rico/8/1934 PR8) in A549 cells pre-treated with interferon α2a. The assay was performed as described previously  with commercially-available interferon α2a (produced in E. coli) as a control. The egg white interferon showed improved activity compared to the commercial protein (Fig. 1f), calculated to be as high as 1 × 109 U/mg, an order of magnitude greater than the bacterially-produced protein.
Simple purification of high quality, biologically active porcine growth factor-Fc fusion protein
Egg white from pCSF1-Fc eggs was clarified of ovomucin as described for interferon purification. All of the protein came through in the supernatants (Fig. 2d). The active dimer form of pCSF1-Fc was purified by MabSelect SuRe capture followed by size exclusion chromatography (SEC) polishing, and purity confirmed by SDS-PAGE (Fig. 2e). Due to the difficulty in quantifying pCSF1-Fc in whole egg white by western blot and the lack of an ELISA test, concentration of protein was calculated based on the final recovery and estimates of protein loss through the purification process based on western blots of samples collected throughout the process (Fig. 2f). Purity was > 97%, as determined by reversed phase chromatography and SEC-multi-angle light scattering. The molecular mass average across the elution profile is 95.1 kDa with good protein mono-dispersity (Mw/Mn = 1.011) and no significant aggregation. Co-polymer model analysis indicated that peak mass was comprised of 85.6 kDa of protein and 9.5 kDa of oligosaccharide (~ 10% glycosylation). (Additional file 5: Figure S5). Mass spectrometry analysis confirmed the identity of pCSF1-Fc; presence of contaminating egg white proteins was below the limit of detection (Additional file 6: Table S1). The Ba/F3 cell survival assay was repeated with pCSF1-Fc purified from fresh egg white, egg white that had been stored at -20 °C for at least 1 month, and egg white that had been stored at -80 °C for at least 1 month. The control pCSF1-Fc and all purified egg pCSF1-Fc samples were able to promote cell survival at comparable levels (Fig. 2g), demonstrating that egg white can be collected and frozen for a significant period of time prior to purification without loss of recovery or activity. The ability of the purified protein to interact with the native CSF1 receptor was confirmed using mouse bone marrow cells. Both control and egg-derived pCSF1-Fc promoted cell differentiation at comparable levels (Fig. 2h).
Validation of the Fc-fusion approach by production of a potential human therapeutic cytokine
These results indicate that both interferon α2a and CSF1-Fc are efficiently synthesized as a component of egg white, readily recoverable using common chromatography methods, and biologically active in vitro and in vivo at levels equal to control cytokines produced in different systems.
Lentiviruses are efficient vectors for the generation of transgenic chickens with stable germline transmission and consistent, oviduct-specific expression of correctly folded and functional protein . Here we have demonstrated an improved promoter design that generated levels of expression compatible with cost-effective scale-up. There were no negative effects on the health of the hens despite the substantial increase in expression of exogenous protein. The method can be applied to untagged and Fc-tagged proteins, and common chromatographic techniques can be applied to purify the proteins from egg white. Initial characterization of egg-derived proteins showed high levels of purity and activity as good as or better than the equivalent proteins produced in traditional cell culture or E. coli systems. Contamination by egg proteins was below levels detectable by mass spectrometry and in vivo testing showed no immunogenic reaction in mice. It is likely that similarly-structured proteins, including the many therapeutic Fc fusion proteins currently under clinical evaluation [23, 24]. will be amenable to production in the egg white of transgenic chickens and purification as we have described at commercially relevant scale.
The infrastructure and upstream costs of a transgenic chicken bioreactor production system are predicated to be substantially lower than those for mammalian cell culture, perhaps by as much as two orders of magnitude, due largely to the comparably lower cost of chicken facilities and lack of requirement for GMP conditions until egg crack. Initial analysis provided by the Centre for Process Innovation National Biologics Manufacturing Centre (Darlington, UK) indicates that downstream processing costs should be equivalent to current methods, leading to an overall lower manufacturing cost. Relative to mammalian transgenic animal bioreactors, a flock of bioreactor chickens is faster and cheaper to produce, and egg white is a simpler mixture of proteins with a significantly lower lipid content than milk. In addition, the favorable glycosylation patterns and oxidative environment of the chicken system make it appealing for production of proteins with specific requirements for these characteristics that are currently difficult to recapitulate in cell culture.
The lentivirus system was the best available at the time of generation of these chicken lines, but since then, significant advances have taken place in chicken primordial germ cell culture and genome editing. Combining these techniques means precise control over the insertion site of the transgene and uniformity of the resulting chicken population. It also means substantially increased efficiency, reduced need for genotype screening, no biosafety concerns around lentiviral particles, and overall lower upstream line generation costs, making the transgenic chicken bioreactor an even more appealing option.
Human interferons were amongst the first patented biologicals. The extension of many of the therapeutic applications of human interferon α2a (RoferonA) and other isoforms to companion animal veterinary medicine have been reviewed recently . Interferon also has increased bioavailability as a Fc fusion protein , and this form would be even more readily produced in a chicken bioreactor using the purification approach described here. Production in chickens may bring the cost down to levels that would support wider applications, and extension to containment of viral diseases in valuable livestock. For the CSF1-Fc fusion protein, a dose of 1 mg/kg twice a week was required to produce a maximal elevation of blood monocyte and tissue macrophage numbers when tested in pigs . Presuming similar efficacy in humans, a single dose could be obtained from 2 to 3 eggs. One of the therapeutic applications of CSF1-Fc already validated in mouse models is in the treatment of bone fractures , an application of relevance to both human and companion animal medicine. Even if production of proteins such as CSF1-Fc in chickens faces hurdles in translation to the human clinic, the bioreactor will enable cost-effective production of the amounts required to test clinical applications in informative large animal models.
We have demonstrated that a human cytokine, interferon α2a, can be recovered at a level of 15 mg/100 ml egg white (the approximate volume from 3 eggs) with biological activity estimated as 1 × 109 IU/mg. In addition, we have generated two transgenic lines in which porcine and human CSF1 have been synthesized as FC fusion proteins. Very high recovery (80–90%) from ~ 100 mg/100 ml of highly pure proteins with biological activity comparable to equivalent proteins produced in cell culture was demonstrated. We have validated the transgenic chicken system for the cost-effective production of pure, high quality, biologically active proteins for therapeutics and other applications.
Construction of transgenes
The human interferon α2a coding sequence was codon-optimized for chicken and synthesized with a Kozak consensus sequence, start codon and chicken lysozyme signal peptide at the 5′ end. The synthetic gene was ligated into a replication defective vector derived from equine infectious anemia virus (EIAV) containing a 4.4 kb modified form of the EREOVA promoter and regulatory elements (EREOVA2) previously shown to drive protein expression restricted to the hen oviduct . The original EREOVA promoter had 0.9 kb deleted between the estrogen-responsive enhancer element (ERE) and the steroid-dependent regulatory element (SDRE) that was preserved in EREOVA2. The new promoter was found to enhance protein expression in egg white at least 10-fold compared to EREOVA. The synthesized, codon-optimized gene for pCSF1-Fc (Entelechon, Germany) consisted of a Kozak sequence, start codon, lysozyme signal peptide and 154 amino acid active form of porcine CSF1 joined to the hinge-CH3 region of porcine IgG1a as previously described (13). This transgene was cloned using designed restriction sites AatII and NheI into a modified pLenti6/DEST Gateway vector, with the V5 tag removed and downstream oPRE added. This vector was derived from human immunodeficiency virus (HIV) and contained the EREOVA2 promoter.
Production of transgenic birds
The birds were derived from a flock of Novagen Brown commercial egg layer strain. Lentiviral vectors were packaged and injected into embryos from new-laid eggs to generate G0 transgenic birds . Cockerels estimated by PCR analysis to have vector sequence present in the germ line at frequency of > 1% were bred with wild-type hens to generate G1 birds, which were screened by PCR and Southern transfer analysis to confirm that the complete gene was present as a single copy. Egg white from G1 hens or female G2 offspring of G1 cockerels was tested for presence of transgene-derived protein. Lines were established from validated G1/G2 birds for each transgene.
Protein expression analysis
Protein expression was demonstrated by SDS-PAGE and western blot. Samples were prepared by addition of 4x NuPAGE LDS sample buffer, and 10x sample reducing agent for gels that were run under reducing conditions and heated at 70 °C for 10 min before gel electrophoresis using Novex NuPAGE 12% Bis-Tris/MOPS gels (Life Technologies). Proteins were transferred onto nitrocellulose membranes by use of an XCell II Blot Module (Life Technologies). Transfer was verified by Ponceau S staining and membranes were blocked overnight at 4 °C. For westerns imaged using the LI-COR scanner, blocking was performed with Odyssey Blocking Buffer, while for westerns visualized using HRP, blocking was performed with 5% (w/v) powdered milk in TBS. Interferon α2a was detected with monoclonal anti-interferon α (Sigma, UK, catalogue number SAB1409236) at 1:1000 dilution and sheep anti-mouse IgG conjugated HRP (GE Healthcare NXA931-1ML) or LI-COR IRDye 680RD Donkey anti-Rabbit IgG (H + L) at 1:20,000 dilution and imaged with a LI-COR Odyssey Imager according to manufacturer’s instructions. Concentration was estimated with a commercial ELISA kit according to manufacturer’s instructions (PBL Biomedical Laboratories 41,100). Due to a lack of antibody against porcine CSF1, CSF1-Fc was immunoblotted with anti-porcine Fc conjugated to HRP (Bethyl Laboratories A100-104P) at a 1:10,000 dilution in 3% (w/v) powdered milk in TBS 0.1% (v/v) Tween-20. Interferon concentration was determined by quantitative Western blot using LI-COR Image Studio software.
Egg white activity analysis
Whole egg white from transgenic hens’ eggs was tested for activity prior to purification. For interferon, the ability to stimulate interferon-stimulated response element (ISRE)-driven transcription of luciferase was used to determine initial whole egg white activity. The pGL4.45[luc2P/ISRE/Hygro] vector (Promega) was transfected in HEK293T cells seeded in white-walled 96-well plates at 1 × 104 cells/well using FuGENE HD (Promega) according to manufacturer’s instructions. 24 h post-transfection, the medium was replaced with antibiotic-free medium and either egg white from transgenic hens or wild type egg white with control interferon protein (Sigma) added at an estimated final concentration of 10 international units (IU), 102 IU and 104 IU, with diluted wild type egg white used as a negative control. After a further 24 h, the One Glo Luciferase assay kit (Promega) was used to measure luminescence according to manufacturer’s instructions. For pCSF1-Fc, a cell survival assay based upon the ability of viable cells to reduce 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium bromide (MTT) was performed as previously described . Briefly, stable Ba/F3 cells expressing porcine CSF1 receptor were grown in complete RPMI (10% (v/v) fetal calf serum, penicillin, streptomycin, and GlutaMAX) and supplemented with 5% (v/v) X63 cell supernatant from X63 Ag8–653 myeloma cells carrying an expression vector for IL-3 (22). Cells were seeded in 96-well plates at a density of 2 × 104 cells/well in triplicate and treated with serial dilutions of egg or CHO cell-produced pCSF1-Fc instead of IL-3, with negative controls containing complete RPMI with no X63 or pCSF1-Fc. Plates were incubated at 37 °C, 5% (v/v) CO2 for 48 h and MTT (Sigma) at a final concentration of 0.5 mg/mL was added for a further 3-h incubation, followed by solubilization overnight with acidified isopropanol. Absorbance was measured at 570 nm and results normalized to the highest dose positive control.
Protein purification and analysis
For pCSF1-Fc and hCSF1-Fc purification, egg white was diluted 1:4 in 50 mM phosphate buffer pH 3, adjusted to pH 4, and stirred at room temperature for 10 min to precipitate ovomucin. The diluted egg white was centrifuged at 25,000 g for 45 min at 10 °C, the supernatant adjusted to pH 7 and centrifuged again at 25,000 g for 45 min at 10 °C to remove any further precipitates. The clarified egg white was diluted to a final volume of 10 times the original egg white volume and pCSF1-Fc was bound to a 5 mL HiTrap MabSelect SuRe column (GE Healthcare) pre-equilibrated with 50 mM phosphate buffer, pH 7, (PB) at 5 mL/min by use of an Äkta Prime Plus liquid chromatography system (GE Healthcare). The column was washed with 10 column volumes of PB and the protein was eluted with 3–5 column volumes of 100 mM citrate buffer (CB) pH 3, or until the UV peak had returned to baseline, into tubes containing 1 M Tris pH 9 at 30% of the final fraction volume. The column was regenerated with 3 column volumes of CB and 5 column volumes of PB, cleaned in place with 5 column volumes of 0.5 M NaOH, pH adjusted with 5 column volumes of PB and finally cleaned with 10 column volumes of 20% (v/v) ethanol for storage. The fractions containing eluted protein, as determined by SDS-PAGE, were pooled and concentrated to < 13 mL in an Amicon stirred cell with 10,000 Da ultrafiltration regenerated cellulose membrane and injected onto a Superdex 200 26/600 column (GE Healthcare) equilibrated with PBS at 2.5 mL/min by use of the Äkta Prime Plus. Fractions were collected manually to ensure that only the main portion of the correct peak was isolated. After use the column was cleaned with 1–2 column volumes of 20% (v/v) ethanol and stored.
For Interferon α2a, egg white was diluted 1:4 in 20 mM phosphate buffer pH 3, adjusted to pH 4, and stirred at room temperature for 10 min to precipitate ovomucin. The diluted egg white was then centrifuged at 25,000 g for 45 min at 10 °C, the supernatant adjusted to pH 7 and centrifuged again at 25,000 g for 35 min at 10 °C to remove any further precipitates. The clarified egg white was diluted to a final volume of 10 times the original egg white volume and interferon α2a was bound onto a 5 mL HiTrap Blue column (GE Healthcare) equilibrated with 20 mM PB pH 7 at 5 mL/min by use of an Äkta Prime Plus liquid chromatography system (GE Healthcare). The column was washed with 10 column volumes of PB and protein eluted with 20 mM PB containing 1 M NaCl. The fractions containing interferon α2a, as determined by SDS-PAGE, were pooled, diluted to 10 times the pooled volume in ddH2O to prevent salt-induced association of interferon and ovalbumin, concentrated to < 13 mL in an Amicon stirred cell with 10,000 Da ultrafiltration regenerated cellulose membrane and injected onto a Superdex 200 26/600 column (GE Healthcare) equilibrated with PBS at 2.5 mL/min by use of the Äkta Prime Plus. After use the column was cleaned with 1–2 column volumes of 20% (v/v) ethanol and stored. Interferon-containing fractions, as determined by SDS-PAGE, were concentrated by Amicon filtration. Protein concentration was determined by UV280. Identity was confirmed by SDS-PAGE and mass spectrometric analyzes (Roslin Proteomics and Metabolomics Facility) and quality was assessed by reversed phase chromatography and SEC-multi-angle light scattering at the Edinburgh Protein Production Facility (EPPF), Kings Buildings, Edinburgh.
Analysis of purified Interferon α2a activity
A dose-inhibition assay was performed to determine interferon activity compared to a commercially available control (Sigma SRP4594). HEK 293 T cells were used to produce influenza A/PR/8/34 (PR8) virus as described previously (17). A549 cells were pre-treated with varying concentrations of interferon for 24 h, then infected at low multiplicity (MOI 0.001). After 1 h of adsorption at 37 °C, virus-containing medium was replaced with virus growth medium (DMEM, 1 μg/mL TPCK-treated trypsin, 0.14% (w/v) BSA). After 48 h, virus was harvested and titer determined by plaque assay on MDCK cells with an Avicel overlay (virus growth medium supplemented with 1.2% (v/v) Avicel) followed by toluidine blue staining (17, 23). The virus titer was normalized to a no-interferon control to determine dose-inhibition.
Analysis of purified pCSF1-Fc activity
In vitro activity of purified egg pCSF1-Fc was tested by the MTT assay in Ba/F3 cells as described for whole egg white, and in pig bone marrow cells as previously described . Briefly, pig bone marrow cells were derived from pigs culled by captive bolt at Dryden farm as previously described [31, 38]. Cells were plated at 5 × 104 cells/well in a 96-well plate directly from frozen stocks and grown in complete RPMI supplemented with either CHO-derived or egg purified pCSF1-Fc at 10 ng/mL, 100 ng/mL or 1000 ng/mL. After 7 days, the culture medium was replaced with 50 μl of 1 mg/ml MTT solution and incubated for 1 h at 37 °C. The MTT solution was removed and tetrazolium salt solubilized with 100 μl of solubilization agent (0.1 M HCL, 10% Triton X-100 and isopropanol) followed by incubation at 37 °C with 5% CO2 for 10 min. Plates were read at 570 nm.
In vivo activity of pCSF1-Fc was tested in mice as previously described . Approval was obtained from The Roslin Institute’s and The University of Edinburgh’s Protocols and Ethics Committees. The experiments were carried out under the authority of a UK Home Office Project License under the regulations of the Animals (Scientific Procedures) Act 1986. Twelve male C57BL/6 mice aged 6–8 weeks were purchased from Charles River Laboratories (UK) and injected subcutaneously with either PBS, 1 mg/kg pCSF1-Fc from CHO cells or 1 mg/kg pCSF1-Fc from eggs (n = 4 per group) for 4 days and sacrificed on day 5 by rising levels of carbon dioxide. Liver and spleen were removed, weighed and fixed in 10% neutral buffered formalin for histological analysis. Blood was collected by cardiac puncture and transferred into EDTA-coated tubes, then prepared for flow cytometry using the Uti-Lyse kit (Dako, Ely, UK) and stained with PE anti-mouse F4/80 (Biolegend, CA, USA, catalogue number 122616, 1:200) and APC anti-mouse Mac1/CD11b (Abcam, Cambridge, UK, catalogue number ab25482, 1:2000) to identify the macrophage population. Results were analyzed with FlowJo software.
Analysis of purified hCSF1-Fc activity
Activity of purified egg hCSF1-Fc was tested by the bone marrow MTT assay as described for pCSF1-Fc. To test whether the protein could withstand drying for long-term storage and easier shipping, aliquots of protein were brought to dryness using a Savant SPD2010 Speedvac (Thermo) at a constant vacuum pressure of 5.1 Torr over 1.5-h without heating. The protein was reconstituted in the same volume of ddH2O and used as described for pCSF1-Fc in the bone marrow differentiation assay.
Analysis was performed with GraphPad Prism Version 6.04 and statistical significance was assessed using Student’s two-tailed t-test. Resulting values were considered statistically significant at p < 0.05.
We thank Dr. E. Eliot, Dr. C. Robertson and colleagues at the former Viragen Inc. for their contributions to the early stages of developing the ovalbumin promoter-human interferon α2a transgenic line. We thank the Centre for Process Innovation National Biologics Manufacturing Centre for cost of goods analysis and assistance with protein downstream processing. We thank the staff of the Transgenic Chicken Facility and Greenwood Poultry Unit for the breeding and husbandry of the transgenic lines. We thank the staff of the Biological Resource Facility for assistance in carrying out the experiments on mice.
This work was supported by BBSRC strategic funding to The Roslin Institute BBS/E/D/20221658, BBSRC grants BB/I013113/1 (in collaboration with Zoetis, Inc.), BB/M021920/1, and BBSRC-University of Edinburgh IAA award; the EPPF is supported by the Wellcome Trust Multi-User Equipment grants 081287/Z/06/Z, 101527/Z/13/Z and the Wellcome-UoE ISSF award; M.L.T. and N.S. were supported by BBSRC grant BB/J01446X/1 and MRC grant MR/K000276/1 (respectively) to P.D. The funding bodies were not involved in the design of the study and collection, analysis, and interpretation of data and in writing the manuscript.
Availability of data and materials
The datasets used and/or analyzed during the current study are available from the corresponding author on reasonable request.
LRH, DAH, HMS and ACG conceived the study. LRH wrote the manuscript with contributions for the different portions of the study as follows: CSF1-Fc protein design, MTT assays and mouse experiments: CP and DAH. Interferon viral assays: MLT, NS and PD. Preparative chromatography: ACG and GP. Analytical chromatography: MW. Promoter and lentiviral construct design and transgenic chicken generation: HMS, SL, AS, and HJG. Mass spectrometry: DK. LRH generated the CSF1-Fc chicken lines with assistance from AS and HJG. SL generated the interferon chicken line with assistance from AS and HJG in collaboration with Viragen Inc. LRH and CP performed mouse experiments. LRH performed protein purification experiments with advice and assistance from ACG and GP. MLT, NS and PD designed, performed and analyzed influenza virus assays; LRH and GP performed CSF1-Fc activity assays with advice from CP. MW and DK performed chromatographic and mass spectrometry (respectively) analysis of purified protein. All authors approved the final version of the manuscript and agreed to be accountable for all aspects of the work in ensuring that questions related to the accuracy or integrity of any part of the work are appropriately investigated and resolved.
Approval for animal experiments was obtained from The Roslin Institute’s and The University of Edinburgh’s Protocols and Ethics Committees. The experiments were carried out under the authority of a UK Home Office Project License under the regulations of the Animals (Scientific Procedures) Act 1986.
Consent for publication
D.A.H. holds a patent position on the applications of CSF1-Fc in liver disease, and of CSF1 in kidney regeneration. Part of this work was performed on a collaborative grant part-funded by Zoetis, Inc. L.R.H. is now employed by Roslin Technologies, who will be commercializing the chicken platform, as well as the current proteins for use as research reagents.
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
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