Different immunity elicited by recombinant H5N1 hemagglutinin proteins containing pauci-mannose, high-mannose, or complex type N-glycans.

Highly pathogenic avian influenza H5N1 viruses can result in poultry and occasionally in human mortality. A safe and effective H5N1 vaccine is urgently needed to reduce the pandemic potential. Hemagglutinin (HA), a major envelope protein accounting for approximately 80% of spikes in influenza virus, is often used as a major antigen for subunit vaccine development. In this study, we conducted a systematic study of the immune response against influenza virus infection following immunization with recombinant HA proteins expressed in insect (Sf9) cells, insect cells that contain exogenous genes for elaborating N-linked glycans (Mimic) and mammalian cells (CHO). While the antibody titers are higher with the insect cell derived HA proteins, the neutralization and HA inhibition titers are much higher with the mammalian cell produced HA proteins. Recombinant HA proteins containing tri- or tetra-antennary complex, terminally sialylated and asialyated-galactose type N-glycans induced better protective immunity in mice to lethal challenge. The results are highly relevant to issues that should be considered in the production of fragment vaccines.

Fed-batch CHO cell t-PA production and feed glutamine replacement to reduce ammonia production.

Industrial therapeutic protein production has been greatly improved through fed-batch development. In this study, improvement to the productivity of a tissue-plasminogen activator (t-PA) expressing Chinese hamster ovary (CHO) cell line was investigated in shake flask culture through the optimization of the fed-batch feed and the reduction of ammonia generation by glutamine replacement. The t-PA titer was increased from 33 mg/L under batch conditions to 250 mg/L with daily feeding starting after three days of culture. A commercially available fed-batch feed was supplemented with cotton seed hydrolysate and the four depleted amino acids, aspartic acid, asparagine, cysteine, and tyrosine. The fed-batch operation increased the generation of by-products such as lactate and ammonia that can adversely affect the fed-batch performance. To reduce the ammonia production, a glutamine-containing dipeptide, pyruvate, glutamate, and wheat gluten hydrolysate, were investigated as glutamine substitutes. To minimize the lag phase as the cells adjusted to the new energy source, a feed glutamine replacement process was developed where the cells were initially cultured with a glutamine containing basal medium to establish cell growth followed by feeding with a feed containing the glutamine substitutes. This two-step feed glutamine replacement process not only reduced the ammonia levels by over 45% but, in the case of using wheat gluten hydrolysate, almost doubled the t-PA titer to over 420 mg/L without compromising the t-PA product quality or glycosylation pattern. The feed glutamine replacement process combined with optimizing other feed medium components provided a simple, practical, and effective fed-batch strategy that could be applied to the production of other recombinant therapeutic proteins.

Protein-free fed-batch culture of non-GS NS0 cell lines for production of recombinant antibodies.

Presented is a novel antibody production platform based on the fed-batch culture of recombinant, NS0-derived cell lines. A standardized fed-batch cell culture process was developed for five non-GS NS0 cell lines using enriched and optimized protein-free, cholesterol-free, and chemically defined basal and feed media. The process performed reproducibly and scaled faithfully from the 2-L to the 100-L bioreactor scale achieving a volumetric productivity of > 120 mg/L per day. Fed-batch cultures for all five cell lines exhibited significant lactate consumption when the cells entered the stationary or death phase. Peak and final lactate concentrations were low relative to a previously developed fed-batch process (FBP). Such low lactate production and high lactate consumption rates were unanticipated considering the fed-batch culture basal medium has an unconventionally high initial glucose concentration of 15 g/L, and an overall glucose consumption in excess of 17 g/L. The potential of this process platform was further demonstrated through additional media optimization, which has resulted in a final antibody concentration of 2.64 +/- 0.19 g/L and volumetric productivity of > 200 mg/L per day in a 13-day FBP for one of the five production cell lines. Use of this standardized protein-free, cholesterol-free NS0 FBP platform enables consistency in development time and cost effectiveness for manufacturing of therapeutic antibodies.