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使用填充床生物反应器从稳定的包装细胞系生产慢病毒载体。

Lentiviral Vector Production from a Stable Packaging Cell Line Using a Packed Bed Bioreactor.

作者信息

Powers Alicia D, Drury Jason E, Hoehamer Christopher F, Lockey Timothy D, Meagher Michael M

机构信息

Department of Therapeutics Production & Quality, St. Jude Children's Research Hospital, Memphis, TN 38105-3678, USA.

Children's GMP, LLC, Memphis, TN, USA.

出版信息

Mol Ther Methods Clin Dev. 2020 Aug 14;19:1-13. doi: 10.1016/j.omtm.2020.08.010. eCollection 2020 Dec 11.

DOI:10.1016/j.omtm.2020.08.010
PMID:32995355
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC7490643/
Abstract

Self-inactivating lentiviral vectors (LVVs) are used regularly for genetic modification of cells, including T cells and hematopoietic stem cells for cellular gene therapy. As vector demand grows, scalable and controllable methods are needed for production. LVVs are typically produced in HEK293T cells in suspension bioreactors using serum-free media or adherent cultures with serum. The iCELLis® is a packed-bed bioreactor for adherent or entrained cells with surface areas from 0.53 to 500 m. Media are pumped through the fixed bed and overflows, creating a thin film that is replenished with oxygen and depleted of CO as media return to the reservoir. We describe the optimization and scale-up of the production of GPRTG-EF1α-hγ-OPT LVV using a stable packaging cell line in the iCELLis Nano 2-cm to the 10-cm bed height low compaction bioreactors (0.53 and 2.6 m surface area) and compare to the productivity and efficacy of GPRTG-EF1α-hγ-OPT LVV manufactured under current Good Manufacturing Practice (cGMP) using 10-layer cell factories for the treatment of X-linked severe combined immunodeficiency. By optimizing fetal bovine serum (FBS) concentration, pH post-induction, and day of induction, we attain viral yields of more than 2 × 10 transducing units/mL. We compared transduction efficiency between LVVs produced from the iCELLis Nano and cell factories on healthy, purified CD34 cells and found similar results.

摘要

自失活慢病毒载体(LVV)常用于细胞的基因改造,包括用于细胞基因治疗的T细胞和造血干细胞。随着载体需求的增长,需要可扩展且可控的生产方法。LVV通常在悬浮生物反应器中的HEK293T细胞中使用无血清培养基生产,或在含血清的贴壁培养物中生产。iCELLis®是一种用于贴壁或夹带细胞的填充床生物反应器,表面积从0.53到500平方米。培养基被泵入固定床并溢出,形成一层薄膜,当培养基返回储液器时,该薄膜会补充氧气并耗尽二氧化碳。我们描述了在iCELLis Nano 2厘米至10厘米床高的低压实生物反应器(表面积0.53和2.6平方米)中使用稳定包装细胞系生产GPRTG-EF1α-hγ-OPT LVV的优化和放大过程,并与使用10层细胞工厂按照现行药品生产质量管理规范(cGMP)生产用于治疗X连锁严重联合免疫缺陷的GPRTG-EF1α-hγ-OPT LVV的生产率和效力进行比较。通过优化胎牛血清(FBS)浓度、诱导后pH值和诱导天数,我们获得了超过2×10转导单位/毫升的病毒产量。我们比较了iCELLis Nano和细胞工厂生产的LVV对健康纯化的CD34细胞的转导效率,结果相似。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/7ada906a1451/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/eb8cea1e1b3c/fx1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/aae1f15a1b58/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/ea86cbdfd224/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/5106fcf6f880/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/85fa9f6fb108/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/7ada906a1451/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/eb8cea1e1b3c/fx1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/aae1f15a1b58/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/ea86cbdfd224/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/5106fcf6f880/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/85fa9f6fb108/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/5954/7490643/7ada906a1451/gr5.jpg

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