Kateja Nikhil, Dureja Samit, Rathore Anurag S
Department of Chemical Engineering, Indian Institute of Technology Delhi, New Delhi, India.
Department of Chemical Engineering, Indian Institute of Technology Delhi, New Delhi, India.
J Biotechnol. 2020 Oct 10;322:79-89. doi: 10.1016/j.jbiotec.2020.07.008. Epub 2020 Jul 17.
PEGylation of therapeutic proteins has long been recognized as a safe and effective approach to enhance pharmacokinetic properties of proteins by increasing the in-vivo half-life and thereby the bioavailability. Despite all the benefits linked to PEGylation, high cost of PEGylated products has hindered accessibility of these products to patients. Continuous processing offers a solution to this predicament with its proven capability to improve economics without sacrificing product quality. In this study, we report the development of an integrated continuous PEGylation and purification process for a therapeutic protein, PEG-GCSF. The methodology to achieve this consisted of developing the batch PEGylation and purification protocols followed by their conversion into an integrated continuous process. A batch process involving rapid and highly productive PEGylation (reaction completion within one hour of reaction time) followed by cation exchange chromatography was developed. Enabling technologies like coiled flow inversion reactor, inline concentrator and counter-current chromatography, were utilized for the successful conversion of the batch process to continuous mode. The final integrated continuous process consisted of continuous PEGylation in a coiled flow inverter reactor followed by four column continuous counter-current cation exchange chromatography. Continuous chromatography was performed in a novel displacement mode, wherein all the multi-PEGylated impurities were removed in the loading flow-through and the pure mono-PEGylated protein was obtained in a single step salt elution. In combination with our previously established GCSF manufacturing train, the end-to-end continuous manufacturing process starting from inclusion bodies to unformulated PEG-GCSF drug substance was successfully run for 12 h. All attributes were found to be consistent over the period of operation with product purity > 99 % and high molecular weight impurities < 0.5 %. We hope that the current study will lay the foundation for implementation of continuous processing as a method to improve manufacturability of PEGylated therapeutic proteins.
长期以来,治疗性蛋白质的聚乙二醇化一直被认为是一种安全有效的方法,可通过延长体内半衰期从而提高生物利用度来增强蛋白质的药代动力学特性。尽管聚乙二醇化有诸多益处,但聚乙二醇化产品的高成本阻碍了患者获得这些产品。连续加工提供了一种解决这一困境的方法,它已被证明有能力在不牺牲产品质量的情况下提高经济性。在本研究中,我们报告了一种用于治疗性蛋白质聚乙二醇化粒细胞集落刺激因子(PEG-GCSF)的集成连续聚乙二醇化和纯化工艺的开发。实现这一目标的方法包括开发分批聚乙二醇化和纯化方案,然后将其转化为集成连续工艺。开发了一种分批工艺,该工艺包括快速且高产的聚乙二醇化(反应时间在一小时内完成反应),随后进行阳离子交换色谱。利用诸如盘管流反转反应器、在线浓缩器和逆流色谱等使能技术,成功地将分批工艺转化为连续模式。最终的集成连续工艺包括在盘管流反转反应器中进行连续聚乙二醇化,然后进行四柱连续逆流阳离子交换色谱。连续色谱以一种新颖的置换模式进行,其中所有多聚乙二醇化杂质在进样流穿中被去除,纯的单聚乙二醇化蛋白质在一步盐洗脱中获得。结合我们先前建立的粒细胞集落刺激因子(GCSF)生产流程,从包涵体到未配制的聚乙二醇化粒细胞集落刺激因子原料药的端到端连续制造工艺成功运行了12小时。在运行期间发现所有属性均保持一致,产品纯度>99%,高分子量杂质<0.5%。我们希望当前的研究将为实施连续加工奠定基础,作为一种提高聚乙二醇化治疗性蛋白质可制造性的方法。