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通过基于模型的优化比较多柱色谱配置。

Comparison of multi-column chromatography configurations through model-based optimization.

机构信息

TCS Research, Tata Research Development and Design Centre, Tata Consultancy Services, Pune, India.

出版信息

Biotechnol Prog. 2023 Nov-Dec;39(6):e3376. doi: 10.1002/btpr.3376. Epub 2023 Jul 16.

Abstract

Integrated continuous bioprocessing has been identified as the next important phase of evolution in biopharmaceutical manufacturing. Multiple platform technologies to enable continuous processing are being developed. Multi-column counter-current chromatography is a step in this direction to provide increased productivity and capacity utilization to capture biomolecules like monoclonal antibodies (mAbs) present in the reactor harvest and remove impurities. Model-based optimization of two prevalent multi-column designs, 3-column and 4-column periodic counter-current chromatography (PCC) was carried out for different concentrations of mAbs in the feed, durations of cleaning-in-place and equilibration protocols. The multi-objective optimization problem comprising three performance measures, namely, product yield, productivity, and capacity utilization was solved using the Radial basis function optimization technique. The superficial velocities during load, wash, and elute operations, along with durations of distinct stages present in the multi-column operations were considered as decision variables. Optimization results without the constraint on number of wash volumes showed that 3-Column PCC performs better than 4-Column PCC. For example, at a feed concentration of 1.2 mg/mL, productivity, yield and capacity utilization, respectively, were 0.024 mg/mL.s, 0.94, and 0.94 for 3-Column PCC and 0.017 mg/mL.s, 0.87, and 0.83 for 4-column PCC. Similar trends were observed at higher feed concentrations also. However, when the constraint on number of wash volumes is included, 4-Column PCC was found to result in consistent productivity and product yield under different operating conditions but at the expense of reduced capacity utilization.

摘要

集成连续生物处理已被确定为生物制药制造的下一个重要发展阶段。正在开发多种平台技术以实现连续处理。多柱逆流色谱是朝着这个方向发展的一步,旨在提供更高的生产力和产能利用率,以捕获存在于反应器收获物中的生物分子,如单克隆抗体(mAbs),并去除杂质。针对不同浓度的 mAbs 在进料中、不同的原位清洗和平衡协议持续时间,对两种流行的多柱设计(3 柱和 4 柱周期逆流色谱(PCC))进行了基于模型的优化。使用径向基函数优化技术解决了包含三个性能指标的多目标优化问题,即产品收率、生产率和产能利用率。在负载、清洗和洗脱操作期间的表面速度以及多柱操作中各个阶段的持续时间被视为决策变量。在没有限制洗涤体积数的约束下的优化结果表明,3 柱 PCC 比 4 柱 PCC 性能更好。例如,在进料浓度为 1.2mg/mL 时,3 柱 PCC 的生产率、收率和产能利用率分别为 0.024mg/mL.s、0.94 和 0.94,而 4 柱 PCC 的生产率、收率和产能利用率分别为 0.017mg/mL.s、0.87 和 0.83。在更高的进料浓度下也观察到了类似的趋势。然而,当限制洗涤体积数的约束包括在内时,发现 4 柱 PCC 在不同操作条件下可实现一致的生产率和产品收率,但代价是降低了产能利用率。

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