Trace levels of the CHO host cell protease cathepsin D caused particle formation in a monoclonal antibody product

中国仓鼠卵巢细胞 单克隆抗体 蛋白酶 化学 组织蛋白酶D 蛋白酵素 组织蛋白酶 碎片(计算) 组织蛋白酶B 生物化学 抗体 分子生物学 色谱法 生物 受体 生态学 免疫学
作者
Jared S. Bee,Tie Liu,Douglas S. Johnson,Mariana N. Dimitrova,Kristin C. Jusino,Christopher D. Afdahl
出处
期刊:Biotechnology Progress [American Chemical Society]
卷期号:31 (5): 1360-1369 被引量:88
标识
DOI:10.1002/btpr.2150
摘要

Chinese hamster ovary (CHO) cells are often used to produce therapeutic monoclonal antibodies (mAbs). CHO cells express many host cell proteins (HCPs) required for their growth. Interactions of HCPs with mAbs can sometimes result in co‐purification of trace levels of ‘hitchhiker’ HCPs during the manufacturing process. Purified mAb‐1 product produced in early stages of process optimization had high HCP levels. In addition, these lots formed delayed‐onset particles containing mAb‐1 and its heavy chain C‐terminal fragments. Studies were performed to determine the cause of the observed particle formation and to optimize the purification for improved HCP clearance. Protease activity and inhibitor stability studies confirmed that an aspartyl protease was responsible for fragmentation of mAb‐1 resulting in particle formation. An affinity resin was used to selectively capture aspartyl proteases from the mAb‐1 product. Mass spectrometry identified the captured aspartyl protease as CHO cathepsin D. A wash step at high pH with salt and caprylate was implemented during the protein A affinity step to disrupt the HCP–mAb interactions and improve HCP clearance. The product at the end of purification using the optimized process had very low HCP levels, did not contain detectable protease activity, and did not form particles. Spiking of CHO cathepsin D back into mAb‐1 product from the optimized process confirmed that it was the cause of the particle formation. This work demonstrated that process optimization focused on removal of HCPs was successful in eliminating particle formation in the final mAb‐1 product. © 2015 American Institute of Chemical Engineers Biotechnol. Prog. , 31:1360–1369, 2015
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