Recombinant human insulin. III. High-performance liquid chromatography and high-performance capillary electrophoresis control in the analysis of step-by-step production of recombinant human insulin.

The production of recombinant human insulin consists of five main stages, accompanied by considerable transformation of molecules, concerning size, secondary structure and the presence of charged groups. The application of different methods, i.e., size-exclusion, ion-exchange and reversed-phase high-performance liquid chromatography (HPLC) and high-performance capillary electrophoresis (HPCE) (capillary zone electrophoresis and micellar electrokinetic capillary chromatography), to the analysis of insulin, insulin-related and non-insulin-related substances was studied. A combined HPLC-HPCE system for the step-by-step control of recombinant human insulin production technology is suggested. The advantages and shortcomings of these methods are discussed.

[Preparation of recombinant cytokines. II. Effective method for isolation, purification and renaturation of human recombinant gamma-interferon]. / Metoddy polucheniya rekombinantnykh belkov-tsitokinov. II*. 'Effektivnyl metod vydeleniya irenaturatsii rekombinantrnogo gamma-interferona cheloveka

An efficient method for the isolation, purification, and renaturation of human recombinant gamma-interferon from biomass of transformed E. coli cells was developed. It involves the extraction of the protein from the inclusion bodies, preliminary purification of the protein, and three stages of ion-exchange chromatography with an intermediate renaturation between the second and the third stages. A highly active (2 x 10(7) U/mg) recombinant protein of up to 99% purity (according to SDS-PAGE and HPLC) was obtained with a 30% overall yield.

Recombinant human insulin. V. Optimization of the reversed-phase high-performance liquid chromatographic separation.

The applicability of reversed-phase high-performance liquid chromatography (HPLC) to the analysis of the products of recombinant insulin was studied. The influence of several mobile phases in reversed-phase and ion-pair HPLC on selectivity, resolution and sensitivity was investigated. Optimum conditions for the separation of insulin-related proteins on commercial and laboratory-made supports were established by means of three-dimensional optimizations of selectivity and resolution as a function of pH and ionic strength (mu). A mechanism for the separation of proteins with a mobile phase containing a high salt concentration and a pH near the isoelectric point of proteins is proposed. The questions of scaling up are considered. The proposed techniques allow the analysis of the main impurities and ensures a high quality of active insulin production.

Methods of preparation of recombinant cytokine proteins.

Two schemes for efficient and productive isolation for mutant human recombinant tumor necrosis factor-alpha (TNF-alpha R32H) from Escherichia coli cells were developed. The methods include membrane filtration, ion-exchange chromatography and gel filtration, and centrifugation with subsequent free-flow electrophoresis as an alternative procedure. The target product was obtained as active trimer with total yield more than 50% and greater than 98% purity according to PAGE, size-exclusion chromatography, HPLC, and HPCE.

Recombinant human insulin. VIII. Isolation of fusion protein--S-sulfonate, biotechnological precursor of human insulin, from the biomass of transformed Escherichia coli cells.

Various methods have been investigated for the isolation and purification of fusion proteins of precursors of human insulin in the form of S-sulfonates, from the biomass of transformed Escherichia coli cells. Fusion proteins were prepared with different sizes and structures of the leader peptide and the poly-His position (inserted for purification by metal chelate affinity chromatography). The fusion proteins contained an IgG-binding B domain of protein A from Staphylococcus aureus at the N-terminus and an Arg residue between the leader peptide of the molecule and the proinsulin sequence, for trypsin cleavage of the leader peptide. Six residues of Cys in proinsulin allow the chemical modification of the protein as a (Cys-S-SO(-)(3))(6) derivative (S-sulfonate), which increases its polyelectrolytic properties and improves the efficiency of its isolation. Various methods of oxidative sulfitolysis were compared with catalysis by sodium tetrathionate or cystine and Cu2+ or Ni2+ ions. An optimum scheme for the isolation and purification of S-sulfonated fusion proteins was developed by the combination of metal-chelating affinity and ion-exchange chromatography. Highly purified (95%) S-sulfonated fusion protein was recovered which was 85% of the fusion protein contained in the biomass of E. coli cells. Folding of fusion protein S-sulfonate occurred with high yield (up to 90-95%). We found that the fusion protein-S-sulfonate has proinsulin-like secondary structure. This structure causes highly efficient fusion protein folding.