Downstream processing of human antibodies integrating an extraction capture step and cation exchange chromatography

被引:35
作者
Azevedo, Ana M. [1 ]
Rosa, Paula A. J. [1 ]
Ferreira, I. Filipa [1 ]
de Vries, J. [2 ]
Visser, T. J. [2 ]
Aires-Barros, M. Raquel [1 ]
机构
[1] Univ Tecn Lisboa, Ctr Chem & Biol Engn, IBB Inst Biotechnol & Bioengn, Inst Super Tecn, P-1049001 Lisbon, Portugal
[2] Syncom BV, NL-9747 AT Groningen, Netherlands
来源
JOURNAL OF CHROMATOGRAPHY B-ANALYTICAL TECHNOLOGIES IN THE BIOMEDICAL AND LIFE SCIENCES | 2009年 / 877卷 / 1-2期
关键词
Antibodies; Aqueous two-phase systems; Cation exchange chromatography; Alternative downstream process; Amino acid mimetic ligand; Polyethylene glycol glutaric acid; AQUEOUS 2-PHASE SYSTEMS; MONOCLONAL-ANTIBODIES; PURIFICATION; OPTIMIZATION;
D O I
10.1016/j.jchromb.2008.11.014
中图分类号
Q5 [生物化学];
学科分类号
071010 ; 081704 ;
摘要
In this paper we explore an alternative process for the purification of human antibodies from a Chinese hamster ovary (CHO) cell supernatant comprising a ligand-enhanced extraction capture step and cation exchange chromatography (CEX). The extraction of human antibodies was performed in an aqueous two-phase system (ATPS) composed of dextran and polyethylene glycol (PEG), in which the terminal hydroxyl groups of the PEG molecule were modified with an amino acid mimetic ligand in order to enhance the partition of the antibodies to the PEG-rich phase. This capture step was optimized using a design of experiments and a central composite design allowed the determination of the conditions that favor the partition of the antibodies to the phase containing the PEG diglutaric acid (PEG-GA) polymer, in terms of system composition. Accordingly, higher recovery yields were obtained for higher concentrations of PEG-GA and lower concentrations of dextran. The highest yield experimentally obtained was observed for an ATPS composed of 5.17% (w/w) dextran and 8% (w/w) PEG-GA. Higher purities were however predicted for higher concentrations of both polymers. A compromise between yield and purity was achieved using 5% dextran and 10% PEG-GA. which allowed the recovery of 82% of the antibodies with a protein purity of 96% and a total purity of 63%, determined by size-exclusion chromatography. ATPS top phases were further purified by cation exchange chromatography and it was observed that the most adequate cation exchange ligand was carboxymethyl, as the sulfopropyl ligand induced the formation of multi-aggregates or denatured forms. This column allowed the elution of 89% of the antibodies present in the top phase, with a protein purity of 100% and a total purity of 91%. The overall process containing a ligand-enhanced extraction step and a cation exchange chromatography step had an overall yield of 73%. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:50 / 58
页数:9
相关论文
共 26 条
  • [1] Andrews BA, 1996, BIOSEPARATION, V6, P303
  • [2] [Anonymous], 2006, A comprehensive reference for science, industry, and data mining
  • [3] [Anonymous], SEP PURIF TECHNOL, V215, P528, DOI [10.1016/j.seppur.2019.01.063, DOI 10.1016/J.SEPPUR.2008.07.022, DOI 10.1016/J.SEPPUR.2008.03.06]
  • [4] Optimisation of aqueous two-phase extraction of human antibodies
    Azevedo, Ana M.
    Rosa, Paula A. J.
    Ferreira, I. Filipa
    Aires-Barros, M. Raquel
    [J]. JOURNAL OF BIOTECHNOLOGY, 2007, 132 (02) : 209 - 217
  • [5] High throughput screening techniques in downstream processing: Preparation, characterization and optimization of aqueous two-phase systems
    Bensch, Matthias
    Selbach, Bjorn
    Hubbuch, Juergen
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (07) : 2011 - 2021
  • [6] Membrane adsorbers as purification tools for monoclonal antibody purification
    Boi, Cristiana
    [J]. JOURNAL OF CHROMATOGRAPHY B-ANALYTICAL TECHNOLOGIES IN THE BIOMEDICAL AND LIFE SCIENCES, 2007, 848 (01): : 19 - 27
  • [7] ETZEL M, 2006, PROCESS SCALE BIOSEP, P159
  • [8] Factorial screening of antibody purification processes using three chromatography steps without protein A
    Follman, DK
    Farner, RL
    [J]. JOURNAL OF CHROMATOGRAPHY A, 2004, 1024 (1-2) : 79 - 85
  • [9] *FROST SULL, 2006, BIOT UP STREAM DOWN
  • [10] Frost & Sullivan, 2004, STRAT AN DOWNSTR PRO