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Continuous refolding of a biotech therapeutic in a novel Coiled Flow Inverter Reactor

机译:在新型螺旋流逆变器反应器中生物技术治疗剂的连续折叠

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A novel coiled flow inverter (CFI) based plug flow reactor has been developed for continuous refolding of granulocyte colony stimulating factor (GCSF), a biotech therapeutic product. Solubilized inclusion bodies containing the denatured and reduced forms of GCSF were continuously diluted with the refolding buffer using an inline mixing unit. This was followed by protein refolding into a CFI based tubular reactor in which a helical coil was bent at equidistant right angles to cause flow inversion at each bend. This configuration effectively provided substantial cross sectional mixing while maintaining a favourable distribution of residence time. Design of experiments (DOE) based studies was performed to optimize the refolding protocol with respect to redox conditions, pH and dilution ratio. The performance of the continuous refolding protocol has been compared with an optimized batch refolding protocol. It has been demonstrated that enhanced mixing in CFI allows for operation at higher protein concentrations (0.38 mg/ml as compared to 0.19 mg/ml in batch) and results in comparable purity (84% vs. 83% in batch), thereby resulting in a nearly 15 times increase in productivity. This will result in a significant reduction of costs related to downstream purification as well as no need for the large tank that is otherwise required for dilution based batch refolding. The proposed configuration is likely to perform favourably in other biotech unit operations that require mixing and/or sharp residence time distribution such as precipitation. (C) 2015 Elsevier Ltd. All rights reserved.
机译:已经开发了一种基于新型螺旋流换流器(CFI)的活塞流反应器,用于生物技术治疗产品颗粒细胞集落刺激因子(GCSF)的连续重折叠。使用在线混合装置,用重折叠缓冲液连续稀释含有变性和还原形式的GCSF的增溶包涵体。随后将蛋白质重新折叠到基于CFI的管式反应器中,在该反应器中,螺旋线圈以等距的直角弯曲,从而在每个弯曲处引起流动反转。这种配置有效地提供了充分的横截面混合,同时保持了良好的停留时间分布。进行了基于实验设计(DOE)的研究,以针对氧化还原条件,pH和稀释比优化重折叠方案。连续重折叠协议的性能已与优化的批量重折叠协议进行了比较。已经证明,在CFI中增强的混合可以在更高的蛋白质浓度下操作(0.38 mg / ml,而批量为0.19 mg / ml),并产生可比较的纯度(批量为84%对83%),从而得到生产率提高了将近15倍。这将大大降低与下游纯化有关的成本,并且不需要大型罐,否则需要基于稀释的批次重新折叠。所提出的配置可能在需要混合和/或急剧的停留时间分布(例如沉淀)的其他生物技术单元操作中表现良好。 (C)2015 Elsevier Ltd.保留所有权利。

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