Abstract
Bioseparation techniques exploit the differences of physicochemical or thermodynamic properties between the product and the contaminants. Rapid development of a downstream process, therefore, requires physicochemical and thermodynamic characterization of the components to be separated. In this paper, we investigate whether a generalized thermodynamic interrelation exists among different parameters. For instance activity coefficients, osmotic virial coefficients and the solubility of macromolecules are interrelated to each other. Experimental determination of any one of these parameters can be translated across the boundaries of different separation techniques. A number of downstream separation processes, including size-exclusion chromatography, hydrophobic-interaction chromatography, reversed-phase chromatography, aqueous two-phase separation, crystallization and precipitation, are found to be explained and designed using this generalized thermodynamics. This generalization of thermodynamic properties together with high-throughput experimentation provides a systematic and high-speed approach to bioseparation process development and optimization. The applicability of this approach for bioseparation process design was investigated by a case study on nystatin, a medium-sized biomolecule. The distribution coefficients of nystatin in reversed-phase chromatography showed straightforward relationship with the solubilities at various solvent compositions and the experimental data supported the trend of the relationship.
| Original language | English |
|---|---|
| Pages (from-to) | 268-282 |
| Number of pages | 15 |
| Journal | Fluid Phase Equilibria |
| Volume | 241 |
| Issue number | 1-2 |
| DOIs | |
| Publication status | Published - 15 Mar 2006 |
| Externally published | Yes |
Keywords
- Activity coefficient
- Biomolecule
- Bioprocess design
- Bioseparation
- Nystatin
- Osmotic virial coefficient
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