Improved antibody production in Chinese hamster ovary cells by ATF4 overexpression.

To improve antibody production in Chinese hamster ovary (CHO) cells, the humanized antibody-producing CHO DP-12-SF cell line was transfected with the gene encoding activating transcription factor 4 (ATF4), a central factor in the unfolded protein response. Overexpression of ATF4 significantly enhanced the production of antibody in the CHO DP-12-SF cell line. The specific IgG production rate of in the ATF4-overexpressing CHO-ATF4-16 cells was approximately 2.4 times that of the parental host cell line. Clone CHO-ATF4-16 did not show any change in growth rate compared with the parental cells or mock-transfected CHO-DP12-SF cells. The expression levels of mRNAs encoding both the antibody heavy and light chains in the CHO-ATF4-16 clone were analyzed. This analysis showed that ATF4 overexpression improved the total production and specific production rate of antibody without affecting the mRNA transcription level. These results indicate that ATF4 overexpression is a promising method for improving recombinant IgG production in CHO cells.

Improved production of recombinant human antithrombin III in Chinese hamster ovary cells by ATF4 overexpression.

To improve the production of recombinant human antithrombin III (AT-III) in Chinese hamster ovary (CHO) cells, the genes encoding transcription factors, ATF4 (activating transcription factor 4) and XBP-1s (the spliced form of X-box binding protein 1), which were involved in the mammalian unfolded protein response (UPR), were cloned from CHO-K1 cells. Overexpression of ATF4 significantly enhanced the production of recombinant AT-III in CHO 13D-35D cells. The specific rate of AT-III production in the ATF4-overexpressed CHO 13D-35D cells reached approximately 23 pg/cell/day. After 144 h of incubation, the AT-III concentration in the culture supernatant was twofold greater compared to that observed with parental CHO 13D-35D cells. In contrast, ectopic expression of XBP-1s failed to enhance the production of recombinant AT-III in CHO 13D-35D cells. RT-PCR analysis revealed that high levels of XBP-1s mRNA were present in the CHO cells, regardless of ectopic expression of XBP-1s. Our results indicate that overexpression of the UPR transcription factor ATF4 is a promising means for improving the production of secreted protein pharmaceuticals in CHO cells.

Overexpression of GADD34 enhances production of recombinant human antithrombin III in Chinese hamster ovary cells.

To improve the production of recombinant human antithrombin III (AT-III) in Chinese hamster ovary (CHO) cells, the gene encoding growth arrest and DNA damage inducible protein 34 (GADD34), which is a transcription factor involved in the unfolded protein response (UPR), was cloned from CHO-K1 cells. Overexpression of GADD34 significantly enhanced the production of recombinant AT-III in CHO 13D-35D cells. The specific rate of AT-III production in the GADD34-overexpressing CHO 13D-35D cells reached approximately 28 pg/cell/d. After 144 h of incubation, the AT-III concentration in the culture supernatant was approximately 40% higher than that observed in the case of the parental CHO 13D-35D cells. The mRNA expression, specific activity, and fucosylation of AT-III were not affected by GADD34 overexpression. Overexpression of GADD34 is a promising method of improving the production of secreted protein pharmaceuticals in CHO cells.

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.

Optimization of human serum albumin production in methylotrophic yeast Pichia pastoris by repeated fed-batch fermentation.

An optimization method for repeated fed-batch fermentation was established with the aim of improving the recombinant human serum albumin (rHSA) production in Pichia pastoris. A simulation model for fed-batch fermentation was formulated and the optimal methanol-feeding policy calculated by dynamic programming method using five different methanol-feeding periods. The necessary state variables were collected from the calculated results and used for further optimization of repeated fed-batch fermentation. The optimal operation policy was investigated using the pre-collected state variables by estimating the overall profit per total methanol-feeding time. The calculated results indicated that the initial cell mass from the 2nd fed-batch fermentation on should be set at 35 or 40 g and methanol-feeding time at 264 h. In repeated fed-batch fermentation using the optimal operation policy, actual culture volume was in good agreement with the values simulated by model equations, but some discrepancy was observed in rHSA production. Minimum experiments were therefore carried out to re-evaluate rHSA production levels, which were then applied in re-calculations to determine the optimal operation policy. The optimal policy for repeated fed-batch fermentation established in the present study (i.e., 4-times-repeated fed-batch fermentation) achieved a 47% increase in annual rHSA production. Optimization of the culture period also brought about a 28% increase in annual rHSA production even in simple (not repeated) fed-batch fermentation.

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.