Enhanced aggregate separation with Sartobind® Rapid A Protein A membrane in the purification of aggregation-prone antibodies
Background: Aggregates are common byproducts associated with the production of recombinant antibodies, and their removal poses considerable challenges to the downstream purification. When a Protein A column is used for product capture, large aggregates do not bind due to the size-exclusion effect, whereas small aggregates (e.g., dimers) co-bind with monomers. Although small aggregates bind marginally stronger than the monomer, the difference is usually too small to effect an effective separation of these two species. Thus, Protein A column chromatography generally lacks the ability to separate monomers from co-binding small aggregates. Recently, Protein A membrane has emerged as a promising alternative to resin-based Protein A columns. Objective: This study aimed to evaluate the potential of Sartobind® Rapid A Protein A membrane’s monomer-aggregate separation. Methods: A Protein A column and a Sartobind® Rapid A membrane were used to separately process five culture harvests containing a high percentage of aggregates, and their performances were compared. Aggregate clearance was monitored by analysing relevant elution fractions using size-exclusion chromatography-high-performance liquid chromatography. Results: Sartobind® Rapid A membrane showed stronger aggregate separation capability than the resin-based Protein A column and effectively removed most aggregates in all feed materials. Conclusion: Sartobind® Rapid A membrane outperforms resin-based Protein A columns for antibodies and Fc-fusion proteins with aggregate-rich harvests. By removing most of the aggregates at the capture stage, Sartobind® Rapid A membrane significantly alleviates the purification burden on polishing steps.
- Vázquez-Rey M, Lang DA. Aggregates in monoclonal antibody manufacturing processes. Biotechnol Bioeng. 2011;108(7):1494-1508. doi: 10.1002/bit.23155
- Li W, Prabakaran P, Chen W, Zhu Z, Feng Y, Dimitrov DS. Antibody aggregation: Insights from sequence and structure. Antibodies (Basel). 2016;5(3):19. doi: 10.3390/antib5030019
- van der Kant R, Karow-Zwick AR, Van Durme J, et al. Prediction and reduction of the aggregation of monoclonal antibodies. J Mol Biol. 2017;429(8):1244-1261. doi: 10.1016/j.jmb.2017.03.014
- Li Y. A brief introduction of IgG-like bispecific antibody purification: Methods for removing product-related impurities. Protein Expr Purif. 2019;155:112-119. doi: 10.1016/j.pep.2018.11.011
- Andrade C, Arnold L, Motabar D, et al. An integrated approach to aggregate control for therapeutic bispecific antibodies using an improved three column Mab platform-like purification process. Biotechnol Prog. 2019;35(1):e2720. doi: 10.1002/btpr.2720
- Chen SW, Zhang W. Current trends and challenges in the downstream purification of bispecific antibodies. Antib Ther. 2021;4(2):73-88. doi: 10.1093/abt/tbab007
- Ingavat N, Dzulkiflie N, Liew JM, et al. Investigation on environmental factors contributing to bispecific antibody stability and the reversal of self-associated aggregates. Bioresour Bioprocess. 2024;11(1):82. doi: 10.1186/s40643-024-00796-y
- Schanzer J, Jekle A, Nezu J, et al. Development of tetravalent, bispecific CCR5 antibodies with antiviral activity against CCR5 monoclonal antibody-resistant HIV-1 strains. Antimicrob Agents Chemother. 2011;55(5):2369-2378. doi: 10.1128/AAC.00215-10
- Hober S, Nord K, Linhult M. Protein A chromatography for antibody purification. J Chromatogr B Analyt Technol Biomed Life Sci. 2007;848(1):40-47. doi: 10.1016/j.jchromb.2006.09.030
- Shukla AA, Hubbard B, Tressel T, Guhan S, Low D. Downstream processing of monoclonal antibodies – application of platform approaches. J Chromatogr B Analyt Technol Biomed Life Sci. 2007;848(1):28-39. doi: 10.1016/j.jchromb.2006.09.026
- Bolton GR, Mehta KK. The role of more than 40 years of improvement in Protein A chromatography in the growth of the therapeutic antibody industry. Biotechnol Prog. 2016;32(5):1193-1202. doi: 10.1002/btpr.2324
- Yuan G, Qu M, Geng Q, Dong W, Zhang X, Li Y. Antibody aggregation can lead to reduced Protein A binding capacity and low step yield. Protein Expr Purif. 2023;210:106315. doi: 10.1016/j.pep.2023.106315
- Liu C, Tian M, Dong W, et al. SEC-HPLC analysis of column load and flow-through provides critical understanding of low Protein A step yield. Protein Expr Purif. 2024;216:106418. doi: 10.1016/j.pep.2023.106418
- Yu D, Song Y, Huang RY, et al. Molecular perspective of antibody aggregates and their adsorption on Protein A resin. J Chromatogr A. 2016;1457:66-75. doi: 10.1016/j.chroma.2016.06.031
- Zhang Y, Wang Y, Li Y. A method for improving Protein A chromatography’s aggregate removal capability. Protein Expr Purif. 2019;158:65-73. doi: 10.1016/j.pep.2019.02.017
- Yigzaw Y, Hinckley P, Hewig A, Vedantham G. Ion exchange chromatography of proteins and clearance of aggregates. Curr Pharm Biotechnol. 2009;10(4):421-426. doi: 10.2174/138920109788488842
- Xu Z, Li J, Zhou JX. Process development for robust removal of aggregates using cation exchange chromatography in monoclonal antibody purification with implementation of quality by design. Prep Biochem Biotechnol. 2012;42(2):183-202. doi: 10.1080/10826068.2012.654572
- Lu Y, Williamson B, Gillespie R. Recent advancement in application of hydrophobic interaction chromatography for aggregate removal in industrial purification process. Curr Pharm Biotechnol. 2009;10(4):427-433. doi: 10.2174/138920109788488897
- Gao D, Wang LL, Lin DQ, Yao SJ. Evaluating antibody monomer separation from associated aggregates using mixed-mode chromatography. J Chromatogr A. 2013;1294:70-75. doi: 10.1016/j.chroma.2013.04.018
- Waller JA, Zheng J, Dyer R, et al. Ceramic hydroxyapatite chromatography plays a critical role in bispecific antibody purification process for impurity removal. Antib Ther. 2022;6(1):30-37. doi: 10.1093/abt/tbac030
- Ingavat N, Wang X, Liew JM, et al. Harnessing ceramic hydroxyapatite as an effective polishing strategy to remove product- and process-related impurities in bispecific antibody purification. Bioresour Bioprocess. 2023;10(1):93. doi: 10.1186/s40643-023-00713-9
- Rupčíková V, Molnár T, Kurák T, Polakovič M. Antibody aggregate removal by multimodal chromatography. Molecules. 2025;30(11):2363. doi: 10.3390/molecules30112363
- Busse RA, Gruenberg M, Kuchemueller KB, Toeppner K, Adametz P, Thom V. Sartobind Rapid A: Comparable high product quality as Protein A resins at high productivity. Application Note; 2022. Available from: https://www. sartorius.hr/media/3u2fwqe3/sartobind-rapid-a-comparable-high-product-quality-as-protein-a-resins-at-high-productivity. pdf [Last accessed on 2025 Oct 01].
- Grünberg M, Kuchemüller KB, Töppner K, Busse RA. Scalable, robust and highly productive novel convecdiff membrane platform for mAb capture. Membranes. 2022;12(7):677. doi: 10.3390/membranes12070677
- Osuofa J, Husson SM. Comparative evaluation of commercial Protein A membranes for the Rapid purification of antibodies. Membranes. 2023;13(5):511. doi: 10.3390/membranes13050511
- Yang S, Braczkowski R, Chen SH, et al. Scalability of Sartobind Rapid A membrane for high productivity monoclonal antibody capture. Membranes. 2023;13(10):815. doi: 10.3390/membranes13100815
- Gehrmann N, Daxbacher A, Hahn R. Rapid purification of mAb using Protein A membranes yielding high HCP clearance. J Chromatogr B Analyt Technol Biomed Life Sci. 2024;1232:123989. doi: 10.1016/j.jchromb.2023.123989
- Lu W, Zhang T, Wan Y, Li Y. Protein A membrane shows an advantage over Protein A resin in purifying antibodies/Fc-fusions forming noncovalent aggregates. Chromatogr Sep Tech J. 2024;4:127.
- Yuan G, Qu M, Li Y. Effective and robust separation of half-antibody byproduct in bispecific antibody purification by Sartobind Rapid A Protein A membrane chromatography. Protein Expr Purif. 2026;237:106823. doi: 10.1016/j.pep.2025.106823
