Leuchs Barbara, Frehtman Veronika, Riese Markus, Müller Marcus, Rommelaere Jean
German Cancer Research Center Tumor Virology F010, Im Neuenheimer Feld 280, 69120, Heidelberg, Germany.
Appl Microbiol Biotechnol. 2017 Apr;101(8):3143-3152. doi: 10.1007/s00253-016-8071-x. Epub 2017 Jan 14.
The rodent protoparvovirus H-1PV, with its oncolytic and oncosuppressive properties, is a promising anticancer agent currently under testing in clinical trials. This explains the current demand for a scalable, good manufacturing practice-compatible virus purification process yielding high-grade pure infectious particles and overcoming the limitations of the current system based on density gradient centrifugation. We describe here a scalable process offering high purity and recovery. Taking advantage of the isoelectric point difference between full and empty particles, it eliminates most empty particles. Full particles have a significantly higher cationic charge than empty ones, with an isoelectric point of 5.8-6.2 versus 6.3 (as determined by isoelectric focusing and chromatofocusing). Thanks to this difference, infectious full particles can be separated from empty particles and most protein impurities by Convective interaction media diethylaminoethyl (DEAE) anion exchange chromatography: applying unpurified H-1PV to the column in 0.15 M NaCl leaves, the former on the column and the latter in the flow through. The full particles are then recovered by elution with 0.25 M NaCl. The whole large-scale purification process involves filtration, single-step DEAE anion exchange chromatography, buffer exchange by cross-flow filtration, and final formulation in Visipaque/Ringer solution. It results in 98% contaminating protein removal and 96% empty particle elimination. The final infectious particle concentration reaches 3.5E10 plaque forming units (PFU)/ml, with a specific activity of 6.8E11 PFU/mg protein. Overall recovery is over 40%. The newly established method is suitable for use in commercial production.
啮齿动物细小病毒H-1PV具有溶瘤和抑瘤特性,是一种目前正在临床试验中进行测试的很有前景的抗癌药物。这就解释了目前对一种可扩展的、符合药品生产质量管理规范的病毒纯化工艺的需求,该工艺能够产生高纯度的纯感染性颗粒,并克服基于密度梯度离心的现有系统的局限性。我们在此描述一种可扩展的工艺,该工艺具有高纯度和高回收率。利用完整颗粒和空颗粒之间的等电点差异,它可以去除大多数空颗粒。完整颗粒的阳离子电荷明显高于空颗粒,其等电点为5.8 - 6.2,而空颗粒为6.3(通过等电聚焦和层析聚焦测定)。由于这种差异,感染性完整颗粒可以通过对流相互作用介质二乙氨基乙基(DEAE)阴离子交换色谱与空颗粒和大多数蛋白质杂质分离:将未纯化的H-1PV以0.15M NaCl溶液上样到柱中,前者保留在柱上,后者则流出。然后用0.25M NaCl洗脱回收完整颗粒。整个大规模纯化过程包括过滤、单步DEAE阴离子交换色谱、错流过滤进行缓冲液交换以及最终在碘克沙醇/林格氏溶液中进行制剂配制。该工艺可去除98%的污染蛋白和96%的空颗粒。最终感染性颗粒浓度达到3.5E10空斑形成单位(PFU)/ml,比活性为6.8E11 PFU/mg蛋白。总体回收率超过40%。新建立的方法适用于商业生产。