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首页> 外文期刊>Biotechnology Progress >Theoretical Analysis of Excipient Concentrations During the Final Ultrafiltration/Diafiltration Step of Therapeutic Antibody
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Theoretical Analysis of Excipient Concentrations During the Final Ultrafiltration/Diafiltration Step of Therapeutic Antibody

机译:治疗性抗体最终超滤/渗滤步骤中赋形剂浓度的理论分析

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Diafiltration of a protein solution into a new buffer is a common final step in biopharma-ceutical manufacturing. However,the excipient concentrations in the retentate are not always equal to their corresponding concentrations in the new buffer (diafiltration buffer). This phenomenon was observed repeatedly during diafiltration of different therapeutic monoclonal antibodies in which the concentrations of histidine and either sorbitol or sucrose (depending on which was chosen for the diafiltration buffer) in the retentate were lower than in the diafiltration buffer. Experimental studies and theoretical analyses of the ultrafiltration/ diafiltration (UFIDF) step were carried out to determine the primary causes of the phenomenon and to develop a mathematical model capable of predicting retentate excipient concentrations. The analyses showed that retentate histidine concentration was low primarily because of repulsive charge interactions between positively-charged histidine molecules and positively-charged protein molecules,and that volume exclusion effects were secondary for like-charged molecules. The positively-charged protein molecules generate an electrical potential that cause an uneven distribution of charged histidine molecules. This interaction was used to construct a mathematical model based on the Poisson-Boltzmann equation. The model successfully predicted the final histidine concentration in the diafiltered product (retentate) from the UFIDF development and production runs,with good agreement across a wide range of protein and histidine concentrations for four therapeutic monoclonal antibodies. The concentrations of uncharged excipients (sorbitol or sucrose) were also successfully predicted using previously established models,with volume exclusion identified as the primary cause of differences in uncharged excipient concentrations in the retentate and diafiltration buffer.
机译:将蛋白质溶液渗滤到新的缓冲液中是生物制药生产中常见的最终步骤。但是,保留物中赋形剂的浓度并不总是等于新缓冲液(渗滤缓冲液)中相应的浓度。在渗滤不同治疗性单克隆抗体的过程中反复观察到此现象,其中保留物中组氨酸和山梨糖醇或蔗糖(取决于渗滤缓冲液的选择)的浓度低于渗滤缓冲液中的浓度。对超滤/渗滤(UFIDF)步骤进行了实验研究和理论分析,以确定该现象的主要原因,并建立了能够预测渗余赋形剂浓度的数学模型。分析表明,滞留组氨酸的浓度较低主要是由于带正电的组氨酸分子与带正电的蛋白质分子之间的排斥性相互作用,而体积排阻作用对带正电的分子是次要的。带正电的蛋白质分子产生的电势导致带电的组氨酸分子分布不均。这种相互作用被用来基于Poisson-Boltzmann方程构建数学模型。该模型通过UFIDF的开发和生产运行成功地预测了渗滤产品(截留液)中的最终组氨酸浓度,对于四种治疗性单克隆抗体而言,在广泛的蛋白质和组氨酸浓度范围内均具有良好的一致性。使用先前建立的模型还可以成功预测不带电荷的赋形剂(山梨糖醇或蔗糖)的浓度,体积排阻被确定为渗余液和渗滤缓冲液中不带电荷的赋形剂浓度差异的主要原因。

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