Cost-effective purification process development for chimeric hepatitis B core (HBc) virus-like particles assisted by molecular dynamic simulation.

Inserting foreign epitopes to hepatitis B core (HBc) virus-like particles (VLPs) could influence the molecular conformation and therefore vary the purification process. In this study, a cost-effective purification process was developed for two chimeric HBc VLPs displaying Epstein-Barr nuclear antigens 1 (EBNA1), and hepatitis C virus (HCV) core. Both chimeric VLPs were expressed in soluble form with high production yields in Escherichia coli. Molecular dynamic (MD) simulation was employed to predict the stability of chimeric VLPs. HCV core-HBc was found to be less stable in water environment compared with EBNA1-HBc, indicating its higher hydrophobicity. Assisting with MD simulation, ammonium sulfate precipitation was optimized to remove host cell proteins with high target protein recovery yields. Moreover, 99% DNA impurities were removed using POROS 50 HQ chromatography. In characterization measurement, we found that inserting HCV core epitope would reduce the ratio of α-helix of HCV core-HBc. This could be another reason on the top of its higher hydrophobicity predicted by MD simulation, causing its less stability. Tertiary structure, transmission electron microscopy, and immunogenicity results indicate that two chimeric VLPs maintained correct VLP structure ensuring its bioactivity after being processed by the developed cost-effective purification approach.

A highly efficient integrated chromatographic procedure for the purification of recombinant hepatitis B surface antigen from Hansenula polymorpha.

The high expression level of recombinant hepatitis B surface antigen obtained from Hansenula polymorpha yeast cell (Hans-HBsAg) made it possible to produce HBsAg vaccine in a large scale and by cost-effective process. However, the present available purification process was somewhat tedious, time-consuming and difficult to scale up. To improve the purification efficiency and simplify the purification process, an integrated chromatographic process was developed and optimized. The downstream process included ion-exchange chromatography (IEC), hydrophobic interaction chromatography (HIC) and gel filtration chromatography (GFC). A series of chromatographic adsorbents were evaluated for their performances on the purification of Hans-HBsAg, and then the suitable adsorbents for IEC and HIC were screened out, respectively. After clarification by centrifugation, the supernatant of cell disruption (SCD) was purified by standard chromatographic steps, IEC on DEAE Sepharose FF, HIC on Butyl-S-QZT and GFC on Sepharose 4FF. Furthermore, HBsAg recovery, purification factor (PF) and purity during the downstream process were evaluated with enzyme-linked immunosorption assay (ELISA), sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS-PAGE) and high-performance size-exclusion chromatography (HPSEC). The results demonstrated that in the scale of 550ml SCD, the total HBsAg recovery and PF of the whole procedure were about 21.0+/-0.9% and 80.7+/-8.4 (n=3) respectively, with the purity of above 99%. This new downstream process was efficient, reproducible and relatively easy to be scaled up.