Process development for the recovery and purification of recombinant protein G

J Biotechnol. 1992 Nov;26(2-3):213-29. doi: 10.1016/0168-1656(92)90008-w.

Abstract

The domains of protein G from streptococcus which bind immunoglobulin G have been cloned and expressed in Escherichia coli (Fahnestock et al., 1986). Because protein G binds to several animal immunoglobulin G's, it has many immunochemical applications. This report describes process development for large-scale production of this recombinant protein G (also known as GammaBind G). In 200 l cultures of E. coli, this protein G variant was released from the cell into the culture medium by heating at 80 degrees C for 10 min. The concentration was monitored by either a competitive enzyme-linked immunoassay or a liquid chromatographic assay. Cross-flow microfiltration with 0.22 micron membrane was used to remove the cells. The protein G-rich permeate from the cross-flow microfilter was purified by affinity chromatography using a 5 l column of IgG-Sepharose 6 Fast Flow, which yielded 16-18 g of protein G per column cycle. The pools of purified protein G were concentrated and desalted using ultrafiltration. The salt-free protein G was then lyophilized as bulk product. The overall recovery through the entire process was 50-64%. The analysis of the final product included sodium dodecyl sulfate polyacrylamide gel electrophoresis, UV-visible spectrum, high performance gel filtration, endotoxin level and binding efficiency to human IgG Sepharose.

MeSH terms

  • Bacterial Proteins / analysis
  • Bacterial Proteins / isolation & purification*
  • Chromatography, Affinity
  • Immunoglobulin G / chemistry*
  • Recombinant Proteins / analysis
  • Recombinant Proteins / isolation & purification*
  • Streptococcus / chemistry*
  • Ultrafiltration

Substances

  • Bacterial Proteins
  • IgG Fc-binding protein, Streptococcus
  • Immunoglobulin G
  • Recombinant Proteins