期刊文献+

应用于抗体药物捕获的耐碱亲和层析介质性能的比较

Comparison of performances of alkaline-resistant affinity chromatographic media for capture of therapeutic antibodies
原文传递
导出
摘要 目的比较应用于抗体药物捕获的耐碱的4种蛋白A亲和层析介质和2种小分子亲和层析介质的性能,为单抗纯化工艺的选择提供参考。方法利用两种单抗纯品(mAb1和mAb2)测定4种蛋白A亲和层析介质MabSelectSuRe、POROS MabCaptureA、Absolute High Cap、TOYOPEARL AF-rProtein A-650F和2种小分子亲和层析介质Mabsorbent A2P HF、Fabsorbent F1P HF在停留时间分别为4、6、8 min时的动态载量;利用含mAb2的发酵液,从回收率和杂质去除方面比较6种亲和层析介质的纯化效果。结果在5%穿透点,各介质对mAb1和mAb2的动态载量在35~73 g/L之间。小分子亲和层析介质Mabsorbent A2P HF纯化mAb2的回收率为89%,其他5种介质纯化mAb2的回收率均≥96%;6种介质纯化mAb2的宿主细胞蛋白(host cell protein,HCP)在2 000 ppm之内,蛋白A残留量在20 ppm之内。结论结合流速、动态载量、回收率和杂质去除效果等指标,可从6种亲和层析介质中挑选适用于抗体类药物下游纯化工艺的耐碱型蛋白A或小分子亲和介质。 Objective To compare the performances of four alkaline-resistant protein A affinity chromatographic media and two small molecular affinity chromatographic media,and provide a reference for selection of purification procedure for monoclonal antibodies(mAbs). Methods The dynamic binding capacities(DBCs)of four protein A affinity chromatographic media MabSelectSuRe,POROS MabCaptureA,Absolute High Cap and TOYOPEARL AF-rProtein A-650F as well as two small molecular affinity chromatographic media Mabsorbent A2P HF and Fabsorbent F1P HF were determined by plotting breakthrough curves of two purified monoclonal antibodies(mAb1 and mAb2)with retention times of 4,6 and 8 min,respectively. The performance of these six affinity media,including recovery rate and removal of foreign matters,were further investigated with clarified cell culture supernatant containing mAb2. Results At 5% breakthrough point,the DBCs of these media were 35 ~ 73 g / L. The recovery rate of mAb2 by Mabsorbent A2P HF was 89%,while those by other five media were not less than 96%. The residual host cell protein(HCP)contents in mAb2 purified by the six media were less than 2 000 ppm,while the residual protein A contents were less than 20 ppm. Conclusion Taking into consideration of flow rate,DBC,recovery rate and removal of foreign matters,alkaline-resistant protein A or small molecular affinity chromatographic media suitable for downstream purification process of therapeutic antibodies may be selected from the six affinity chromatographic media.
出处 《中国生物制品学杂志》 CAS CSCD 2014年第5期695-699,共5页 Chinese Journal of Biologicals
关键词 单克隆抗体 纯化 亲和层析 介质 Monoclonal antibody Purification Affinity chromatography Medium
  • 相关文献

参考文献10

  • 1Top 20 best-selling drugs of 2012:which drugs were the biggest hits last year[OL].Genet Eng Biotechnol News.[2013-07-30].http://www.genengnews.com.
  • 2Gottschalk U.Bioseparation in antibody manufacturing:the good,the bad and the ugly[J].Biotechnol Prog,2008,24(3):496-503.
  • 3Ljungberg UK,Jansson B,Niss U,et al.The interaction of different domains of staphylococcal protein A and human polyclonal IgG,IgA,IgM and F(ab′)2:separation of affinity from specificity[J].Mol Immunol,1993,30(14):1279-1285.
  • 4Mahajan E,George A,Wolk B.Improving affinity chromatography resin efficiency using semi-continuous chromatography[J].J Chromatogr A,2012,1227(1):154-162.
  • 5Hagel L,Jagschies G,Sofer G.Handbook of process chro matography:development,manufacturing,validation and economics[M].2nd ed.London UK:Academic Press,2008:147-159.
  • 6Bain B,Brazil M.Adalimumab[J].Nat Rev Drug Discov,2003,2(9):693-694.
  • 7Chhatre S,Titchener-Hooker NJ,Newcombe AR,et al.Purification of antibodies using the synthetic affinity ligand absorbent Mabsorbent A2P[J].Nat Protoc,2007,2(7):1763-1769.
  • 8孙文改,苗景赟.抗体生产纯化技术[J].中国生物工程杂志,2008,28(10):141-152. 被引量:11
  • 9Walker John M.The protein protocols handbook[M].3rd ed.New York USA:Humana Press,2009:1951-1959.
  • 10Pigeon CJ,Jackson M,Baines D.Application of FabsorbentTM F1P HF,a synthetic ligand adsorbent for capture and purification of a single-domain antibody fragment expressed in Escherichia coli[J].BioProcess Int,2009,7(7):90-91.

二级参考文献14

  • 1Pierce L N, Shabram P W. Scalability of a disposable bioreactor from 25L 500L run in perfusion mode with a CHO-based cell line: A tech review. BioProcessing Journal, 2004, 3 (4) :51 - 56
  • 2Hahn R, Shimahara K, Steindl F, et al. Comparison of protein A affinity sorbents Ⅲ. Life time study. Journal of Chromatography A, 2006, 1102 (1- 2 ) : 224 - 231
  • 3Ghose S, Allen M, Hubbard B, et al. Antibody variable region interactions with protein A: implications for the development of generic purification processes. Biotechnol Bioeng, 2005, 92 (6) : 665 -673
  • 4Hahn R, Sehlegel R, Jungbauer A. Comparison of protein A affinity sorbents. J Chromatogr B Analyt Technol Biomed Life Sci, 2003, 790(1 -2): 35-51
  • 5Lee S H, Kim J S. Optimization of buffer conditions for the removal of endotoxins using Q-sepharose. Process Biochemistry, 2003, 38:1091 -1098
  • 6Wilson M J, Haggart C L, Gallagher S P, et al. Removal of tightly bound endotoxin from biological products. Journal of Biotechnology, 2001, 88 (1): 67-75
  • 7Anspach F B,Hilbeck O. Removal of endotoxins by affinity sorbents. Journal of Chromatography A, 1995, 711 ( 1 ) : 81 - 92
  • 8FDA, Points to Consider in Manufacturing and Testing of Monoclonal Antibody Products for Human Use. 1997, Feb. Part Ⅱ. b. 4. c
  • 9Zhou J X, Dermawan S, Solamo F, et al. pH-gradient cation exchange chromatography for process scale antibody purification. The 229th ACS national meeting. 2005 13 -17, San Diego, CA
  • 10中国药品与生物制品检定所.人用单克隆抗体质量控制技术指导原则.2003-3

共引文献10

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部