METHOD FOR PRODUCING BLOOD COAGULATION FACTOR VII, AND BLOOD COAGULATION FACTOR VII
20180148705 · 2018-05-31
Inventors
- Dimas Tadeu Covas (São Paulo, BR)
- Marcela Cristina Corrêa de Freitas (São Paulo, BR)
- Virginia Picanço e Castro (São Paulo, BR)
- Kamilla Swiech (São Paulo, BR)
Cpc classification
C12N7/00
CHEMISTRY; METALLURGY
C12N2740/15043
CHEMISTRY; METALLURGY
C12N2740/16043
CHEMISTRY; METALLURGY
C12N2740/15042
CHEMISTRY; METALLURGY
C12N15/86
CHEMISTRY; METALLURGY
International classification
Abstract
A process for producing blood coagulation factor VII in 3 human cell lines (HepG2, Sk-Hep, HKB-11) and to select the best recombinant protein producer. The murine line BHK-21 was used as control. The data allow to assert that the system used to modify cell lines was efficient, so that all the cells were satisfactorily modified, and produced the protein of interest of stable form. In addition, when comparing the murine line BHK-21 with the human cells (HepG2, Sk-Hep-1 and HKB-11), the latter showed to be able to produce rFVII more efficiently, which allows to conclude that human cell lines are a great alternative for the production of recombinant blood coagulation factors.
Claims
1: A process of producing blood coagulation factor VII comprising the steps of: 1) obtaining virus particles containing FVII and the protein GFP as reporter gene; 2) transducting human cell lines, preferably, SK-Hep 1, HKB11 and HepG 2 with viral particles to form FVII-producing cells; 3) culturing human FVII-producing cells in suspension using microcarriers.
2: The process according to claim 1, wherein step (1) is performed from the transfection of the cell line Hek293T.
3: The process according to claim 2, wherein transfection uses a lentiviral vector containing the transgene and two auxiliary vectors.
4: The process according to claim 2, wherein the transfection uses a polyethylamine reagent and three plasmids are transfected in the following ratio: 10 to 25 ug, preferably 20 g vector with the transgene p1054-rFVII; 10 to 15 ug, preferably 13 g pCMVR8.91; 5 to 10 ug, preferably 7 g pMD2 VSVG.
5: The process according to claim 1, wherein in step (1) factor VII and GFP are not fused, being separated by an IRES element.
6: The process according to claim 1, wherein in step (2) the supernatant produced by Hek293T transfected cells are placed on the cultures of the cell lines, in the presence of 3 to 6 ug/ml polybrene, preferably 5.5 g/ml.
7: The process according to claim 6, wherein 24 hours before transduction, the cells are plated in a concentration of 210.sup.5 cells per well in a 6-well plate and viral concentration of 10 virus/cell was added, based on viral titration values.
8: The process according to claim 1, wherein in step (3) the cells are cultured in culture flasks of 75 cm.sup.2 for expansion, incubated at 37 C. and 5% CO.sub.2 until confluence of 80%, being released with Trypsin-EDTA and inoculated in T-flasks of 75 cm.sup.2; after reaching the number 510.sup.6 cells, are inoculated in a spinner flask already containing culture medium and microcarrier.
9: The process according to claim 8, wherein the microcarrier is Cytodex 3 at the concentration of 3.0 g/L.
10: A coagulation factor VII being produced according to the process of claim 1.
11: The process according to claim 3, wherein the transfection uses a polyethylamine reagent and three plasmids are transfected in the following ratio: 10 to 25 ug, preferably 20 g vector with the transgenep1054-rFVII; 10 to 15 ug, preferably 13 g pCMVR8.91; 5 to 10 ug, preferably 7 g pMD2 VSVG.
12: The process according to claim 2, wherein in step (1) factor VII and GFP are not fused, being separated by an IRES element.
13: The process according to claim 3, wherein in step (1) factor VII and GFP are not fused, being separated by an IRES element.
14: The process according to claim 4, wherein in step (1) factor VII and GFP are not fused, being separated by an IRES element.
15: The process according to claim 11, wherein in step (1) factor VII and GFP are not fused, being separated by an IRES element.
Description
BRIEF DESCRIPTION OF THE FIGURES
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DETAILED DESCRIPTION OF THE INVENTION
[0051] The present invention describes the process of producing blood coagulation factor VII comprising the steps of:
[0052] 1) Obtaining virus particles containing FVII and the GFP protein as reporter geneusing lentiviral vector;
[0053] 2) Transducing human cell lines, preferably, SK-Hep 1, HKB 11, and HepG 2 with viral particles to form FVII-producing cells;
[0054] 3) Culturing human FVII-producing cells in suspension using microcarriers.
[0055] Transfection of the Hek293T cell line to produce viral particles was performed. For viral production it is important that the cell line (Hek293T) stably express the gene for the large SV40 T antigen. In this process it is necessary to use a vector containing the transgene and two auxiliary vectors, which have the origin of replication of SV40, so that after transfection the plasmids within of cells can replicate which increases transcription of the transgene and the production of viral proteins and ultimately viral particles will be secreted in the culture medium.
[0056] For the production of viral particles the reagent polyethylamine (PEI) was used. The three plasmids were transfected into the following proportion: 10 to 20 g vector with transgene (p1054-rFVII), 8 to 15 g pCMVR8.91 (containing HIV-1 gag, pol, ver and tat), 5 to 10 g pMD2 VSVG (encodes the VSV-G shell).
[0057] After transfection (15 to 20 hours) the cells were incubated with cool medium. After 48 hours the supernatant was collected, centrifuged at 450g for 5 minutes at 4 C., filtered (0.45 m filter) for the removal of cell fragments. Aliquots of 1 ml were frozen at 80 C. for determination of viral titer and for use in transduction experiments. Once frozen at 80 C. and thawed (at 37 C.), the infection strength is decreased by about 20 to 40%. However, for standardization of use and for experiments may be replicable, the viral particles were primarily frozen.
[0058] For titration of the viral supernatant, it was initially plated 210.sup.5 Hek293T cells in each well of the 6-well plate. After reaching 80 to 90% confluence, the cells were infected with the supernatant containing p1054-rFVII virus in the following dilutions: 1:1, 1:2 and 1:3, the ratio of viral supernatant being to fresh culture medium. The dilutions were made in duplicate and 5.5 ug/mL polybrene was used.
[0059] After 16 h of infection, the cell medium was changed to fresh medium (DMEM 10% bovine fetal serum). Cells were then cultured for 48 h and after this period were trypsinized and taken to flow cytometry for analysis of the expression of the GFP gene contained in vector p1054-rFVII. With the results obtained by the flow cytometry it was possible to calculate the viral titer.
[0060] Factor VII and GFP are not fused, they are separated by a IRES element; the method further comprises identifying the transduced cells and non-transduced cells by the presence of the GFP protein.
[0061] The supernatant produced by Hek293T cells that were previously transfected and frozen, were thawed and placed on the cultures of the Sk-Hep, HepG2, HKB11 and BHK, in the presence of 5.5 g/mL polybrene. For this, 24 hours before of the transduction, the cells were plated at 210.sup.5 cells per well in the 6-well plate. A virus concentration of 10 virus/cell, based on the values obtained by viral titration. After addition of the viral supernatant, the cells were incubated at 37 C. in a humid atmosphere containing 5% CO.sub.2, and the transduction cycles were repeated for two to three consecutive days, depending on the cell line.
[0062] Initially the cells were cultured in culture flasks of 75 cm.sup.2 for expansion, and incubated at 37 C. and 5% CO.sub.2. After reaching the confluence of approximately 80%, the cells were released with Trypsin-EDTA and inoculated in 75 cm.sup.2 T-flasks. The cellular morphology during expansion was observed with the use of an inverted microscope.
[0063] After reaching the sufficient number of cells (510.sup.6 cells), was inoculated into spinner flask (100 to 150 mL, with work volume of 50 mL) already containing culture medium and microcarrier. The concentration of 2.0 to 4.0 g/L of the Cytodex 3 microcarrier was used. The preparation and sterilization of the microcarriers was performed according to the manufacturer's standards. The experiment was divided into 2 phases: the phase for adhesion and the phase for cell expansion. The duration of the adhesion phase was 6 hours with intermittent agitation: every 30 minutes for 2 minutes. For the expansion phase, constant stirring of 40 rpm was used.
[0064] In order to evaluate the cell adhesion in the microcarriers, samples were taken at each hour for cell density determination in suspension and viability.
[0065] To monitor cell growth during the expansion phase samples were taken every 24 hours for cell quantification and for further analysis of glucose, glutamine, lactic acid and ammonia. Free cells in suspension were quantified using method of exclusion by tripan blue dye. For the cells adhered in the microcarriers, the quantification was determined using of the Crystal Violet method.
[0066] Samples of the cell supernatant were collected, centrifuged and frozen at 20 C. for further ELISA analyzes and biological activity assay.
[0067] The experiment lasted 10 days, and every 3 days photomicrographs were performed under phase contrast microscopy to analysis of the cells adhered to the microcarriers and microscopy of fluorescence, for analysis of GFP expression of adhered cells.
[0068] For the adaptation step, the post-sorting of HKB-11 cell was used. Initially the cells were cultured in 75 cm.sup.2 T-flasks in DMEM-F12 medium containing 10% bovine fetal serum. After reaching the confluence of 90%, the cells were trypsinized with trypsin-EDTA solution and 110.sup.6 cells were plated in 25 cm.sup.2 T-flasks with Free Style medium supplemented with Pluronic, ITS (Insulin, Transferrin and Selenium) and 10% (v/v) Penicillin/Streptomycin, in the absence of bovine fetal serum.
[0069] After 48 h, the cells were picked up, counted and viability observed by trypan blue reagent (0.4%). Again 110.sup.6 viable cells were plated in 25 cm.sup.2 T-flasks with Free Style medium supplemented. This procedure was performed by 5 passages, until the cells were adapted to the growth in serum-free and suspension-free medium.
[0070] This process produces about three times as much FVII protein than an amount of FVII protein normally found in human plasma.
Results
Characterization of Cell Lines
[0071] The human cell lines HepG2, Sk-Hep-1, HKB-11 and BHK-21 murine cell line, were cultured in an attempt to produce a master cell bank and a working cell bank. The cell bank production is of utmost importance because it allows that there is a reproducibility of the experiments over the project development.
[0072] In order to better understand the cell lines used in the present invention, a morphological characterization of the cells, by means of photos under optical microscopy of contrast of phase was performed (
[0073] As can be seen in
[0074] The hybrid cell line HKB-11 is shown in (C), in which can observe that the cells grow adhered and have a more elongated morphology, however, of smaller size, when compared to BHK-21. The Sk-Hep-1 (D) line presents morphology of epithelial cells, according to their origin hepatic adenocarcinoma.
[0075] Besides the morphological characterization, the human cell lines were also characterized in terms of gene expression involved in the -carboxylation process. For this, the real-time PCR quantification of -carboxylase genes and vitamin. K 2,3-epoxide reductase (VKORC1), in addition to the calumenine inhibitory gene (CALU). It was also possible to quantificate mRNA for the gene of endogenous Factor VII, as shown in
[0076] In relation to the genes involved in the -carboxylation process, the HepG2 cell lines is the most expressing -carboxylase and VKORC1. HepG2 cells expressed 251 expression relative units (ERU) of the -carboxylase gene and 305 ERU of the VKORC1 gene. HKB-11 and SK-Hep cells express about 63 ERU and 35 ERU of gene -carboxylase and 144 ERU and 50 ERU of the VKORC1 gene, respectively.
[0077] As observed in the graph, the HepG2 lines were the one which most expressed the inhibitory gene CALU, in the order of 580 ERU, followed by HKB-11 (371 ERU) and SK-Hep (281 ERU) lines.
[0078] In order to select the best cell line for the production of recombinant factor VII, a ratio between the expression of the CALU inhibitory gene and the expression of the genes involved in -carboxylation (Table 1).
TABLE-US-00001 TABLE 1 Ratio between expression of CALU, VKORC1 and -carboxylase Cells Ratio (CALU/VKORC1) Ratio (CALU/-carbox) HepG2 1.90 2.30 SK-Hep 5.54 7.85 HKB-11 2.57 5.82
[0079] As shown in Table 1, the cell line that presented lower ratio between the expression of the inhibitory gene CALU and the -carboxylase and VKORC1 was HepG2, followed by the HKB-11 line.
[0080] After the characterization of the human cell lines, the next step consisted of the cloning of the factor VII gene. In view of the gene expression of the cell lines results, as well as literature data, the mRNA isolation of HepG2 cells was started, for subsequent cDNA production, gene isolation and cloning in the vector of expression.
[0081] Factor VII is a gene that, by the process of alternative splicing, presents 4 variants and one of them is not transcribed. The prevalent form in the normal liver is variant 2, which due to the alternative splicing process, does not contain exon 1b and thus encodes a small signal peptide. Variant 1 contains exon 1b, which thus encodes a longer signal peptide. However, the mature peptide coded by both variants are identical. The third variant shows the absence not only of exon 1b but also of exons 2 and 3 and, in this way, it generates a mature peptide that has no biological activity.
[0082] Thus, it was chosen to acquire the factor VII gene related to variant 2 and continue the experiments. This was cloned in the expression vector p1054-CIGWS. Viral vectors have as main advantage the insertion of the transgene into the DNA of the host cell, with which it passes to stably express the gene of interest.
[0083] The lentiviral vector used in this invention has the WPRE element which increases the efficiency of mRNA transport and processing, which probably contributed to a greater expression of FVII in the human cell lines.
Cloning of the FVII cDNA in a Lentiviral Vector
[0084] After cloning the FVII gene in the p1054 lentiviral vector, which culminated in the generation of p1054-rFVII vector, this vector was used for the production of viral particles. For the production of lentiviral vectors in Hek293T cells in addition to the vector containing the transgene, two other vectors, pCMVR 8.91 and pMD2.VSVG, responsible for the formation of the capsid and viral envelope, respectively, are also required to form viable particles. All vectors used were checked with restriction enzymes for confirmation of integrity.
[0085] With the three vectors checked, the triple co-transfection of the Hek293T cell line for the production of lentivirus using PEI reagent was performed.
[0086] Since the p1054 vector has the green fluorescence protein gene, GFP, it was possible to verify the transfection efficiency of cell line by means of fluorescence microscopy and flow cytometry.
[0087] As shown in
[0088] After generation of the lentivirus producing Hek293T cell line, the next step consisted in collecting the cell supernatant containing the viral particles and titrating the amount of virus with intention to know exactly how many viruses would be used in the next step, the transduction of target cell lines.
[0089] To do so, the protocol previously described was used. 3 different dilutions of the viral supernatant were used and each made in duplicate. After 48 hours of infection, the cells were trypsinized and, since the p1054-rFVII vector has GFP, the percentage of infection can be observed by flow cytometry and subsequent calculation of viral title.
[0090] As shown in
[0091] For the purpose of calculating the viral titer the values for the 1:3 dilution were used. The calculated viral titre was 210.sup.6 virus/ml.
Modified Cell Lines for rFVII Production
[0092] After transduction with the viral supernatant, 4 cell lines modified with the vector p1054-rFVII were obtained, being them BHK-21 (murine), HepG2, Sk-Hep and HKB-11 (human). In order to verify if the modification had taken place satisfactorily, the expression of the GFP marker gene by flow cytometry was observed. As shown in
[0093] In order to verify the success of the modification of the cell lines, photomicrographs in a fluorescence optical microscope were made (
Characterization of Recombinant FVII Produced by Cell Lines Expression of rFVII in Modified Cell Lines
[0094] After confirming the expression of the GFP gene by the flow cytometry and fluorescence microscopy methodologies, the next step consisted of analyzing mRNA expression related to the factor VII gene in human cell lines, HepG2, HKB-11 and Sk-Hep (
[0095] As can be seen in
[0096] These data show not only the efficiency in the modification of the cell lines, as shown by flow cytometry and by fluorescence microscopy, as well as the ability of these lines in expressing the recombinant protein of interest.
Quantification of rFVII in Modified Cell Lines
[0097] In order to quantify the total rFVII (active and non-active) produced by the modified cell lines, the ELISA assay was performed. To quantify the biologically active rFVII (rFVIIa) produced by the modified cell lines, the coagulometric test of prothrombin time (PT) was performed. The results of both tests are shown in Table 2.
TABLE-US-00002 TABLE 2 Quantification of FVIIr by the ELISA and PT assay Samples Elisa (ng/mL) Biological activity HepG2 non-transduced 6.3 Nd HepG2/FVIIr 1176.57 (SD 465.65) 1.02 (SD 0.19) Sk-Hep non- 0.0 Nd transduced Sk-Hep/FVIIr 702.36 (SD 59.42) 2.22 (SD 1.20) HKB-11 non- 0.0 Nd transduced HKB-11/FVIIr 585.44 (SD 128.08) 0.17 (SD 0.05) BHK21 non-transduced 0.0 Nd BHK-21/FVIIr 222.60 (SD 112.71) 0.16 (SD 0.04) Human plasm 500.0 1.0
[0098] As can be seen, the three human cell lines HepG2-rFVII, Sk-Hep-rFVII and HKB-11-rFVII showed amounts of rFVII levels higher than those found in human plasma, of the order of 1.7, 1.5, and 1.35, respectively, showing that these lines are promising for the production of the recombinant protein.
[0099] In relation to actively produced rFVII, Sk-Hep/rFVII is the cell with the ability to produce more biologically active protein, followed by HepG2/rFVII, HKB-11/rFVII and finally the murine cell line BHK-21/rFVII.
Western Blot
[0100] After quantifying the recombinant protein by ELISA and verifying that the cell lines were producing biologically active FVIIr, a Western Blot was carried out in order to observe the size of the protein produced.
[0101] After checking the band pattern on the polyacrylamide gel, blotting was performed. For this, the gel content was transferred to a PVDF membrane and labeled with anti-FVII antibody (
[0102] As it can be seen in
[0103] It can also be observed that cells that have higher mRNA expression related to FVIIr, as well as greater quantification in ELISA, are the cells that present bands of greater intensity in the Western Blot (HepG2-FVIIr on lane 2 and Sk-Hep-1-FVIIr on lane 4). Similarly, cells with lower mRNA expression and lower quantification in the ELISA, present bands related to FVIIr of weaker intensity values in Western Blot (HKB-11-FVIIr on lane 6 and BHK-21-FVIIr on lane 8).
[0104] On lane 9 the Novo Seven that was used as positive control of the reaction can be observed. The higher molecular weight band refers to unactivated single chain FVII (50 KDa), and the lower weight band (20 KDa) refers to the activated FVIIr light chain. The band of 30 KDa, referring to the heavy chain of FVIIr, does not appear in blotting since a monoclonal antibody that does not label this chain specifically was used.
Generation of Homogenous HKB-11/rFVII Cell Population
[0105] As shown previously, the HKB-11 cell line was the one which presented the lowest modification efficiency, after which the transduction only 32% of the cells were expressing the GFP marker gene, whereas the Sk-Hep, HepG2 and BHK-21 expressed 95%, 73% and 80%, respectively.
[0106] After 12 months of culturing, used for the establishment of cell lines, the percentage of cells that expressed GFP was followed (Table 3).
TABLE-US-00003 TABLE 3 Decrease in GFP percentage after 12 months of culture % of GFP after % of GFP after 12 Cell line transduction months of culture Sk-Hep-rFVII 95% 80% HKB-11-rFVII 32% 16% HepG2-rFVII 73% 50% BHK-21-rFVII 80% 64%
[0107] As can be seen in Table 3, the HKB-11 cells were those that presented greater loss in the expression of the GFP marker gene, around 50%.
[0108] With the aim of generating a more homogeneous population and with levels of expression more comparable to other cell lines shown in this invention, the selection of positive GFP HKB-11 cells was performed by cell sorting, which is shown in
[0109] As observed, there was an increase in the number of cells that express GFP on the order of 3.9 times. These data were also confirmed by fluorescence microscopy.
[0110] In addition to the increase in the percentage of positive GFP cells, it was possible to observe an increase in the amount of rFVII produced, when the supernatant was assayed by ELISA test. After a period of 96 hours culture, non-sorting cells were producing 604 ng/mL of rFVII, while the post-sorting cells, cultured under the same conditions, produced 1468 ng/mL. From these results, the following experiments were used, only post-sorting HKB-11/rFVII cells, cited as HKB-11/rFVII.
Characterization of rFVII-Producing Cell Lines
[0111] To date, results have been presented related to the generation of recombinant FVII-producing cell lines, as well as an overall characterization of the protein at the level of expression, biological activity and western blot.
[0112] The following results refer to the characterization of the recombinant cell lines with the intention of selecting the best rFVII producer.
Modified Cell Lines Express rFVII mRNA and -Carboxylation Enzymes
[0113] Initially, mRNA expression analysis was performed related to the factor VII gene and the -carboxylase enzymes, VKORC1 and calumenine.
[0114] In order to analyze the expression profile, only the human cell lines HepG2, HKB-11 and Sk-Hep in four different conditions were used: 1) without transduction and without treatment with vitamin K, 2) without transduction and treated with 5 g/mL vitamin K, 3) transduced with vector 1054-rFVII and without treatment with vitamin K and 4) transduced with 1054-rFVII vector and treated with 5 g/mL vitamin K.
[0115] After analyzing the data, it can be observed that the three human lines presented mRNA expression related to recombinant FVII, after lentiviral vector transduction. When submitted to the treatment with vitamin K for a period of 10 passages in culture, the cells showed a similar expression (HepG2: 164563 URE, HKB-11: 119122 ERU and Sk-Hep: 124919 ERU) showing a stabilization in the expression levels of the recombinant protein (
[0116] It is possible to observe that non-transduced HepG2 cell line, because it is derived from a hepatocarcinoma, expresses levels of endogenous FVII mRNA (as shown above) and that the expression of this endogenous FVII is increased by 480 fold when cells are treated with vitamin K.
[0117] When the expression of the enzymes related to -carboxylation was analyzed, it was possible to observe that there was a difference in the expression levels of -carboxylase enzymes, VKORC1 and the inhibitor calumenine (
[0118] As seen in
[0119] The same pattern of expression can be observed in the cell lines modified with FVII before and after treatment with vitamin K. In the HKB-11-FVII cell line the expression of the VKORC1 mRNA increased 7 fold (from 418 to 2883 ERU), -carboxylase increased 150 fold (from 59 to 8869 ERU) and the expression level of calumenine gene mRNA increased 54 fold (from 318 to 17244 ERU). In the Sk-Hep-1-FVII cells the expression of -carboxylase increased 108-fold (from 41 to 4416 REU) and the expression level of calumenine mRNA increased 54 fold (from 267 to 14331 ERU). In HepG2-FVII cells an increase of expression of VKORC1 (from 2045 to 8491 ERU) was observed, the expression of -carboxylase mRNA increased 58 fold (from 197 to 11443 ERU) and the expression level of of calumenine gene mRNA increased 12 fold (from 1317 to 15621 ERU).
Growth Kinetics of Cell Lines
[0120] With the aim to evaluate the growth profile of recombinant factor VII-producing Sk-Hep, HBK-11 and BHK-21 cell lines the experiments were carried out for a period of 7 days, in duplicate.
[0121]
[0122] With the analysis of
[0123] Then the data from the BHK-21 cell were analyzed (
[0124] The BHK-21 murine line (
Production Kinetics of rFVII in Cell Lines
[0125] In addition to the growth curve, assays in a 100 mm.sup.2 plate with the same cell lines were also performed with the objective to evaluate the production of recombinant factor. VII. To this end, the initial concentration of cells was higher than that used in growth kinetics experiments.
[0126]
[0127] When analyzing the amount of rFVII after the experiment period, it was possible to observe that HepG2 cells showed higher production of recombinant protein, whereas in 24 h had a production of 1227 ng/mL, reaching 1843 ng/mL, after 96 h of culture. As the cells were cultured in. 8 ml of medium, it was possible to produce a total of 14.7 g of rFVII, which corresponds to 29.5 IU.
[0128] Sk-Hep cells had a production of 415 ng/mL in 24 h, reaching a total of 1432 ng/mL after 4 days. The HKB-11 line showed a similar production profile when compared to Sk-Hep, whereas on the first day there was an amount of 435 ng/ml of rFVII and at the end of 96 h it was possible to quantify about 1468 ng/mL. As there was 8 ml of culture medium in the plate, it was possible to produce a total of 11.7 g of rFVII, which corresponds to 23.5 IU of the cells HKB-11 and 11.4 g of rFVII, corresponding to 22.9 IU in Sk-Hep cells.
[0129] The BHK-21 murine cell line was the one with the lowest production of rFVII throughout the experiment, and in 24 hours there were 250 ng/mL and at the end of 96 hours only 449 ng/mL, totaling in 8 mL a production of 3.6 g of rFVII, which corresponds to 7.2 IU.
Production of rFVII in Sk-Hep and HKB-11 Cell Lines in Spinner Flasks
[0130] Analysis of the previous results showed that the HepG2 cells have an extremely slow growth pattern, which made it impossible to use it in the subsequent stage of the work. The lineage BHK-21, of murine origin, is not the focus of the present invention, being used only as a control. In this way, the two FVIIr-producing human cell lines, which were used for subsequent experiments of suspension culture are Sk-Hep-1-FVIIr and HKB-11-FVIIr.
[0131] The experiments were carried out for a period of 10 days to analyze the growth profile, as well as the production of FVIIr in the cell lines growing in suspension using microcarriers in spinner flasks. The experiments were carried out in duplicate and the results are presented as an average of both.
[0132] In analyzing the data it was possible to observe that the Sk-Hep-1-FVIIr cell reached the maximum cellular concentration, in the value of 1.1110.sup.6 cell/mL, on the tenth day of the experiment. The exponential phase of growth occurred between days 1 and 6 and the maximum specific speed of growth (max) was 0.35 day.sup.1.
[0133] During the 10 days of culture it was possible to observe a gradual consumption of glucose, as was to be expected, however, there was no depletion due to 50% changes in the culture medium every 24 hours. In relation to lactate production, it was observed that this reached maximum concentration on the fifth day of culture, with the mean value of 1.25 g/L (
[0134] To illustrate the culture in microcarriers and expression of the GFP marker gene, images were taken with microscopy of phase contrast and fluorescence, as shown in
[0135] In order to quantify the production of FVIIr by the Sk-Hep-1-FVIIr cell an ELISA assay was performed. As shown in
[0136] The kinetics of recombinant protein production were also measured in terms of the amount of biologically active FVIIr which the cells were producing. For Sk-Hep-1 cells, the kinetics of production is shown in
[0137] When analyzing the HKB-11-FVIIr cells, these reached the maximum cell concentration, 1.6110.sup.6 cells/mL, on the ninth day of the experiment. The exponential growth phase occurred between on days 1 and 7 and the maximum specific growth speed (max) was 0.36 day.sup.1.
[0138] As in Sk-Hep-1 cells, over the 10 days of culture it was possible to observe a gradual consumption of glucose, as was expected, however, there was no depletion due to the 50% changes culture medium every 24 hours. Regarding the production of lactate, it was observed that it reached the maximum concentration on the ninth day of culture, with mean value of 0.47 g/L (
[0139] Again, with the aim of illustrating the culture in microcarriers and expression of the GFP marker gene were made images with phase contrast microscopy and fluorescence of the cell HKB-11-FVIIr, as shown in
[0140] The ELISA assay was also performed for the HKB-11 line. As shown in
[0141] The kinetics of recombinant protein production were also measured in terms of the amount of biologically active FVIIr which the cells were producing. For HKB-11-FVIIr cells, the kinetics of production is shown in
Adaptation of Factor VII-Producing HKB-11 Cell Line to Growth in Suspension in Bovine Fetal Serum Free Medium
[0142] Because of the higher productivity, the HKB-11/rFVII cell was selected for the adaptation to the growth in suspension in serum free medium (Free Style), and subsequent culture in bioreactors for production of rFVII in large scale.
[0143] As shown in
[0144] These results show that this cell line is an excellent candidate for rFVII production in bioreactors with bovine fetal serum free medium on industrial scale, as it presents a higher production than the commercially available BHK.