Manufacturing Process Intensification of Adeno-Associated Viral Vectors Type-8 Using Weak Partitioning Chromatography With UV-Based Process Analytical Technology (PAT).

IF 3.6 2区 生物学 Q2 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Garima Thakur,Sheldon Mink,Hanne Bak,Andrew D Tustian
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引用次数: 0

Abstract

Separation of full and empty capsids is a critical step in manufacturing of recombinant adeno-associated viral vector (AAV) based gene therapies. Anion exchange chromatography (AEX) is well-established as a scalable method for full/empty separations. Due to the small differences in surface charge between full and empty capsids, shallow linear gradients of increasing conductivity are commonly used to resolve the two species. However, the resolution is adversely impacted by higher column loading, and most linear gradient processes load at 2e13-2e14 capsids/mL of monolith volume (cp/mL monolith) to achieve full capsid purity targets. With the rapid increase reported in upstream AAV titers up to > 1e12 vg/mL in the bioreactor over the last few years, current downstream purification processes utilizing linear gradient AEX are rapidly approaching scalability limits. This is particularly true for processes utilizing monoliths and membranes which are preferred over resins in AAV purifications due to elimination of pore size diffusion limitations. There is a pressing need for next-generation processes that can load more material in the range of > 1e15 cp/mL, while maintaining operating time and process robustness suitable for GMP manufacturing. This study presents a scalable method for empty/full separations for AAV8 using weak partitioning AEX combined with isocratic elution, demonstrated on CIM QA monoliths which are currently extensively used in the industry for AAV manufacturing. By optimizing load conditions and automating the process with UV-based signals, the strategy achieves > 80% full capsid purity and > 80% genomic yields. Compared to standard linear gradient AEX, the weak partitioning method achieves higher % full capsids as well as higher genomic yield due to combined effects of (i) removal of empty capsids in the flowthrough, (ii) reduction of nonspecific binding interactions as a result of column overloading, and (iii) elimination of peak-cutting by using isocratic elution. The approach enables > 10-fold higher loading per cycle while reducing processing time by 10-fold and is well-suited to rapid cycling or continuous processing operations to support next-generation, high-titer processes.
基于紫外过程分析技术(PAT)的弱分配色谱法制造8型腺相关病毒载体的过程强化。
在制造基于重组腺相关病毒载体(AAV)的基因疗法中,完整衣壳和空衣壳的分离是至关重要的一步。阴离子交换色谱法(AEX)是一种成熟的可扩展的全/空分离方法。由于满衣壳和空衣壳之间的表面电荷差异很小,通常使用增加电导率的浅线性梯度来区分这两种物质。然而,较高的柱载量会对分辨率产生不利影响,大多数线性梯度工艺在2e13-2e14衣壳/mL单体体积(cp/mL单体)时加载以达到完整的衣壳纯度目标。在过去的几年中,随着生物反应器中上游AAV滴度的快速增加,目前使用线性梯度AEX的下游纯化工艺正迅速接近可扩展性极限。在AAV净化中,由于消除了孔径扩散的限制,使用单体和膜的工艺优于树脂,这一点尤其正确。迫切需要能够在> - 1e15 cp/mL范围内加载更多材料的下一代工艺,同时保持适合GMP制造的操作时间和工艺稳健性。本研究提出了一种可扩展的AAV8空/满分离方法,使用弱分区AEX结合等温洗脱,并在目前广泛用于AAV制造行业的CIM QA单体上进行了演示。通过优化负载条件和基于uv信号的自动化过程,该策略实现了> 80%的全衣壳纯度和> 80%的基因组产量。与标准线性梯度AEX相比,弱分配方法实现了更高的全衣壳百分比和更高的基因组产量,这是由于(i)在流动中去除空衣壳,(ii)由于色谱柱超载而减少非特异性结合相互作用,以及(iii)通过使用等差洗脱消除峰切割的综合作用。该方法使>每个周期的负载提高10倍,同时将处理时间缩短10倍,非常适合快速循环或连续处理操作,以支持下一代高滴度工艺。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Biotechnology and Bioengineering
Biotechnology and Bioengineering 工程技术-生物工程与应用微生物
CiteScore
7.90
自引率
5.30%
发文量
280
审稿时长
2.1 months
期刊介绍: Biotechnology & Bioengineering publishes Perspectives, Articles, Reviews, Mini-Reviews, and Communications to the Editor that embrace all aspects of biotechnology. These include: -Enzyme systems and their applications, including enzyme reactors, purification, and applied aspects of protein engineering -Animal-cell biotechnology, including media development -Applied aspects of cellular physiology, metabolism, and energetics -Biocatalysis and applied enzymology, including enzyme reactors, protein engineering, and nanobiotechnology -Biothermodynamics -Biofuels, including biomass and renewable resource engineering -Biomaterials, including delivery systems and materials for tissue engineering -Bioprocess engineering, including kinetics and modeling of biological systems, transport phenomena in bioreactors, bioreactor design, monitoring, and control -Biosensors and instrumentation -Computational and systems biology, including bioinformatics and genomic/proteomic studies -Environmental biotechnology, including biofilms, algal systems, and bioremediation -Metabolic and cellular engineering -Plant-cell biotechnology -Spectroscopic and other analytical techniques for biotechnological applications -Synthetic biology -Tissue engineering, stem-cell bioengineering, regenerative medicine, gene therapy and delivery systems The editors will consider papers for publication based on novelty, their immediate or future impact on biotechnological processes, and their contribution to the advancement of biochemical engineering science. Submission of papers dealing with routine aspects of bioprocessing, description of established equipment, and routine applications of established methodologies (e.g., control strategies, modeling, experimental methods) is discouraged. Theoretical papers will be judged based on the novelty of the approach and their potential impact, or on their novel capability to predict and elucidate experimental observations.
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