RESUMO
Air-liquid interface rings were observed on the side walls of stainless steel buffer vessels after certain downstream buffer preparations. Those rings were resistant to regular cleaning-in-place procedures but could be removed by manual means. To investigate the root cause of this issue, multiple analytical techniques, including liquid chromatography with tandem mass spectrometry detection (LC-MS/MS), high-resolution accurate mass liquid chromatography with mass spectrometry, nuclear magnetic resonance, Fourier transform infrared spectroscopy, and scanning electron microscopy with energy-dispersive X-ray spectroscopy have been employed to characterize the chemical composition of air-liquid interface rings. The main component of air-liquid interface rings was determined to be slip agents, and the origin of the slip agents can be traced back to their presence on raw material packaging liners. Slip agents are commonly used in plastic industry as additives to reduce the coefficient of friction during the manufacturing process of thin films. To mitigate this air-liquid interface ring issue, an alternate liner with low slip agent was identified and implemented with minimal additional cost. We have also proactively tested the packaging liners of other raw materials currently used in our downstream buffer preparation to ensure slip agent levels are appropriate. LAY ABSTRACT: Air-liquid interface rings were observed on the side walls of stainless steel buffer vessels after certain downstream buffer preparations. To investigate the root cause of this issue, multiple analytical techniques have been employed to characterize the chemical composition of air-liquid interface rings. The main components of air-liquid interface rings were determined to be slip agents, which are common additives used in the manufacturing process of thin films. The origin of the slip agents can be traced back to their presence on certain raw material packaging liners. To mitigate this air-liquid interface ring issue, an alternate liner with low slip agent was identified and implemented.
Assuntos
Química Farmacêutica/métodos , Embalagem de Medicamentos/métodos , Preparações Farmacêuticas , Aço Inoxidável , Soluções Tampão , Química Farmacêutica/instrumentação , Cromatografia Líquida/instrumentação , Cromatografia Líquida/métodos , Embalagem de Medicamentos/instrumentação , Espectroscopia de Ressonância Magnética/instrumentação , Espectroscopia de Ressonância Magnética/métodos , Espectrometria de Massas/instrumentação , Espectrometria de Massas/métodos , Preparações Farmacêuticas/síntese química , Espectroscopia de Infravermelho com Transformada de Fourier/instrumentação , Espectroscopia de Infravermelho com Transformada de Fourier/métodos , Propriedades de SuperfícieRESUMO
Extracellular secretion of over 4 g x L(-1) of the A33 scFv antibody fragment was achieved in Pichia pastoris at the 10 L bioreactor scale using minimal medium and feedback control of the methanol concentration. Since methanol acts as both inducer and carbon source, its close regulation is a crucial factor in achieving optimal fermentation conditions. The antibody fragment production levels of both Mut+ and MutS phenotypes were compared in a bioreactor under closed-loop PID control of the methanol level. As expected, the MutS phenotype has a growth rate lower than that of the Mut+ (0.37 vs 1.05 d(-1)) when growing under methanol. However, protein productivity and cell yield on substrate are almost double that of the Mut+ (18.2 vs 9.3 mg A33 sc per gram of methanol). Induction at wet cell weight of 350 g x L(-1) for the MutS also has a positive effect on the final product concentration. Both Mut+ and MutS phenotypes reach a maximum biomass density around 450 g x L(-1) wet cell weight, independent of methanol concentration, reactor scale, or induction density. This reactor configuration allows for reproducible fermentation schemes with different Pichia pastoris phenotypes with AOX promoters, without prior knowledge of the culture growth parameters.
