Nonclinical and quality assessment of cell therapy products: Report on the 4th Asia Partnership Conference of Regenerative Medicine, April 15, 2021.

The 4th Asia Partnership Conference of Regenerative Medicine (APACRM) was held online on April 15, 2021, to promote regulatory harmonization of regenerative medicine products throughout Asia. Recognizing domestic regulatory guidelines within each country and region, and their underpinning rationales, is an important initial step toward a convergence of regulations. The 4th APACRM consisted of an open dialog with regulatory agencies regarding nonclinical and quality settings for cell therapy products (CTPs) through industry presentations and panel discussions with regulatory agencies. The latest updates on regenerative medicine fields in each country and region, and specific regulatory schematics in Japan, were also introduced. The objective of this paper is to summarize the proceedings of the 4th APACRM for public dissemination and to foster further discussion in the future.

Development of a scale-up strategy for Chinese hamster ovary cell culture processes using the kL a ratio as a direct indicator of gas stripping conditions.

Herein, we described a scale-up strategy focused on the dissolved carbon dioxide concentration (dCO2 ) during fed-batch cultivation of Chinese hamster ovary cells. A fed-batch culture process for a 2000-L scale stainless steel (SS) bioreactor was scaled-up from similarly shaped 200-L scale bioreactors based on power input per unit volume (P/V). However, during the 2000-L fed-batch culture, the dCO2 was higher compared with the 200-L scale bioreactor. Therefore, we developed an alternative approach by evaluating the kL a values of O2 (kL a[O2 ]) and CO2 [kL a(CO2 )] in the SS bioreactors as a scale-up factor for dCO2 reduction. The kL a ratios [kL a(CO2 )/kL a(O2 )] were different between the 200-L and 2000-L bioreactors under the same P/V condition. When the agitation conditions were changed, the kL a ratio of the 2000-L scale bioreactor became similar and the P/V value become smaller compared with those of the 200-L SS bioreactor. The dCO2 trends in fed-batch cultures performed in 2000-L scale bioreactors under the modified agitation conditions were similar to the control. This kL a ratio method was used for process development in single-use bioreactors (SUBs) with shapes different from those of the SS bioreactor. The kL a ratios for the SUBs were evaluated and conditions that provided kL a ratios similar to the 200-L scale SS bioreactors were determined. The cell culture performance and product quality at the end of the cultivation process were comparable for all tested SUBs. Therefore, we concluded that the kL a ratio is a powerful scale-up factor useful to control dCO2 during fed-batch cultures.

Development of a chemically defined platform fed-batch culture media for monoclonal antibody-producing CHO cell lines with optimized choline content.

A chemically defined platform basal medium and feed media were developed using a single Chinese hamster ovary (CHO) cell line that produces a monoclonal antibody (mAb). Cell line A, which showed a peak viable cell density of 5.9 × 106 cells/mL and a final mAb titer of 0.5 g/L in batch culture, was selected for the platform media development. Stoichiometrically balanced feed media were developed using glucose as an indicator of cell metabolism to determine the feed rates of all other nutrients. A fed-batch culture of cell line A using the platform fed-batch medium yielded a 6.4 g/L mAb titer, which was 12-fold higher than that of the batch culture. To examine the applicability of the platform basal medium and feed media, three other cell lines (A16, B, and C) that produce mAbs were cultured using the platform fed-batch medium, and they yielded mAb titers of 8.4, 3.3, and 6.2 g/L, respectively. The peak viable cell densities of the three cell lines ranged from 1.3 × 107 to 1.8 × 107 cells/mL. These results show that the nutritionally balanced fed-batch medium and feeds worked well for other cell lines. During the medium development, we found that choline limitation caused a lower cell viability, a lower mAb titer, a higher mAb aggregate content, and a higher mannose-5 content. The optimal choline chloride to glucose ratio for the CHO cell fed-batch culture was determined. Our platform basal medium and feed media will shorten the medium-development time for mAb-producing cell lines.

Development of a fed-batch culture process for enhanced production of recombinant human antithrombin by Chinese hamster ovary cells.

Antithrombin is a serine protease inhibitor that inactivates several coagulation proteases, primarily thrombin and factor Xa. The Chinese hamster ovary (CHO) cell line transfected with a vector expressing recombinant human antithrombin (rAT) and a selectable marker, glutamine synthetase (GS), was cultivated in a 2-l fed-batch culture process using serum-free, glutamine-free medium. To maximize the rAT yield, effects of culture pH, balanced amino acid feeding, and an increased glutamate concentration on cell metabolism and rAT production were investigated. When cells were grown at pH values of 6.6, 6.8, 7.0, and 7.2, the maximum cell density and maximum lactate concentration decreased with decreasing pH. The highest production level of rAT was obtained at culture pH 6.8 due to the extended culture lifetime. Compared to the imbalanced amino acid feeding at culture pH 6.8, the balanced amino acid feeding increased the amount of rAT activity by 30% as a result of an increased viable cell number. A decrease in the specific glucose consumption rate (q(Glc)) with increasing culture time was observed in all the above-mentioned experiments, while the glucose concentration was maintained above 0.7 g l(-1). In addition, a decrease in the specific rAT production rate (q(rAT)) was observed after the depletion of lactate in the late cultivation stage. Taken together, these results suggest that the reduced availability of cellular energy caused by the decrease in q(Glc) and depletion of lactate led to the decrease in q(rAT). This decrease in q(rAT) was partially prevented by increasing the residual glutamate concentration from 1 mM to 7 mM, thus resulting in an additional 30% increase in the amount of rAT activity. The optimized fed-batch culture process yielded 1.0 g l(-1) rAT at 287 h of cultivation.

Production of recombinant human antithrombin by Pichia pastoris.

This paper deals with the production of recombinant human antithrombin (rAT) by the methylotrophic yeast Pichia pastoris. In preliminary methanol-limited fed-batch fermentation, the rAT concentration reached 324 mg/l at 192 h of cultivation, but the specific heparin cofactor (HC) activity of rAT in the culture supernatant was 10% of that of plasma-derived antithrombin (pAT). To improve the specific HC activity of rAT, effort was first focused on the optimization of culture pH and media composition, resulting in protection of rAT against pH-dependent instability and proteolytic degradation. However, even in the optimized methanol-limited fed-batch fermentation, the specific HC activity of rAT in the culture supernatant was still 20% that of pAT. To investigate the unknown mechanisms involved in the decreased specific HC activity of rAT, the culture supernatant of mock-transfected cells was prepared by methanol-limited fed-batch fermentation. When pAT was added to this supernatant, a rapid decrease in HC activity was observed; the residual HC activity was 26% after 24 h of incubation at 25 degrees C. The loss of pAT activity was prevented by addition of a formaldehyde scavenger, amino urea, to the supernatant. In addition, alcohol oxidase activity was observed in the supernatant, resulting in the accumulation of formaldehyde in the culture broth. These results suggest that the formaldehyde produced by methanol oxidation in the culture broth of P. pastoris might decrease the HC activity of rAT during fermentation. Replacing the methanol with glycerol as the carbon source improved the specific HC activity of rAT from 20% to above 40% of that of pAT. In the glycerol-limited fed-batch fermentation, rAT is expressed at 100 mg/l under the control of the truncated mutated AOX2 promoter.

Cloning and characterization in Pichia pastoris of PNO1 gene required for phosphomannosylation of N-linked oligosaccharides.

The yeast Pichia pastoris PNO1 (Phosphomannosylation of N-linked Oligosaccharides) gene, which is involved in phosphomannosylation of N-linked oligosaccharides, was cloned using the Saccharomyces cerevisiae MNN4 gene [Glycobiology 6 (1996) 805] as a probe. The PNO1 open reading frame (ORF) encodes a type II membrane protein composed of 777 amino acid residues. Only in the short region extending from amino acid position 450 to 606 of Pno1p, sequence homology to S. cerevisiae Mnn4p was observed at a level of 45%. The tandem repeat sequence of Lys-Lys-Lys-Lys-Glu-Glu-Glu-Glu characteristic of the C-terminal region of S. cerevisiae Mnn4p is not present in Pno1p. To investigate the function of the PNO1 gene, we constructed a PNO1 gene disruptant by replacement with an expression cassette of human antithrombin (AT), a glycoprotein in plasma. The cell growth and recombinant human antithrombin (rAT) production levels of the disruptant were similar to those of recombinant human antithrombin-expressing wild-type strains. Moreover, the level of alcian blue dye cell staining, which shows the presence of acidic sugar chains on the cell surface, was also similar. However, the phosphomannosylation ratio of N-linked oligosaccharides on recombinant human antithrombin decreased dramatically from 20% in wild-type strains to less than 1% in the PNO1 disruptant. When the PNO1 gene was re-introduced into the disruptant, the phosphomannosylation ratio recovered to the original level. These results suggest that the newly cloned PNO1 gene promotes phosphomannosylation only to core-like oligosaccharides, and not to the hypermannosylated outer chain, and that it has a different function from the MNN4 gene, which promotes the phosphomannosylation of both core and outer sugar chains.

High-level production of prourokinase-annexin V chimeras in the methylotrophic yeast Pichia pastoris.

Prourokinase (proUK)-annexin V chimeras expressed by the methylotrophic yeast Pichia pastoris in a synthetic medium as part of a system designed to yield a novel thrombolytic agent are degraded, as it is thought, by various yeast proteases present in the culture supernatant. Minimization of proteolysis was therefore investigated to increase the yield of intact proUK-annexin V. Protease inhibitor screening study indicated several proteases including at least serine protease like chymotrypsin were involved in the proteolysis. Addition of more than 10% of peptone or more than 0.2 mol l(-1) of arginine to the medium was effective in minimizing proteolysis in shake-flask culture. Culture condition of higher pH was also effective, however, induced a cell death. Cell improvement by increasing the methanol utilization ability yielded greater tolerance to high pH. As a result, the culture condition with highly concentrated peptone solution fed under controlled conditions of pH 8.0 was established, which greatly reduced proteolytic degradation in fed-batch fermentation. These optimal conditions, which enabled fibrinolytic activity to reach 7800 IU ml(-1), could easily be applied in industrial scale production.