High yield refolding and purification process for recombinant human interleukin-6 expressed in Escherichia coli

Citation
D. Ejima et al., High yield refolding and purification process for recombinant human interleukin-6 expressed in Escherichia coli, BIOTECH BIO, 62(3), 1999, pp. 301-310
Citations number
19
Categorie Soggetti
Biotecnology & Applied Microbiology",Microbiology
Journal title
BIOTECHNOLOGY AND BIOENGINEERING
ISSN journal
00063592 → ACNP
Volume
62
Issue
3
Year of publication
1999
Pages
301 - 310
Database
ISI
SICI code
0006-3592(19990205)62:3<301:HYRAPP>2.0.ZU;2-N
Abstract
Recombinant human interleukin-g (hIL-6), a pleiotropic cytokine containing two intramolecular disulfide bonds, was expressed in Escherichia coil as an insoluble inclusion body, before being refolded and purified in high yield providing sufficient qualities for clinical use. Quantitative reconstituti on of the native disulfide bonds of hIL-6 from the fully denatured E. coli extracts could be performed by glutathione-assisted oxidation in a complete ly denaturating condition (6M guanidinium chloride) at protein concentratio ns higher than 1 mg/mL, preventing aggregation of reduced hIL-6. Oxidation in 6M guanidinium chloride (GdnHCl) required remarkably low concentrations of glutathione (reduced form, 0.01 mM; oxidized form, 0.002 mM) to be added to the solubilized hIL-6 before the incubation at pH 8.5, and 22 degrees C for 16 h. After completion of refolding by rapid transfer of oxidized hIL- 6 into acetate buffer by gel filtration chromatography, residual contaminan ts including endotoxin and E. coli proteins were efficiently removed by suc cessive steps of chromatography. The amount of dimeric hIL-6s, thought to b e purification artifacts, was decreased by optimizing the salt concentratio ns of the loading materials in the ion-exchange chromatography, and gradual ly removing organic solvents from the collected fractions of the preparativ e reverse-phase HPLC. These refolding and purification processes, which giv e an overall yield as high as 17%, seem to be appropriate for the commercia l scale production of hIL-6 for therapeutic use. (C) 1999 John Wiley & Sons , Inc.