A refolding chromatography with immobilized molecular chaperonin GroEL was studied for the reactivation of denatured-reduced lysozyme. The effect of denaturant concentration (guanidine hydrochloride, 0.1-1.5M) in the elution buffer, the elution flow-rate, and the loading concentration and volume of the substrate protein on the reactivation yield was studied. All the operating parameters showed minor effects on the recovery yield of lysozyme mass, which remained at 90-100%, but exhibited relatively notable influences on the specific activity of the recovered lysozyme. For example, there existed an optimum denaturant concentration of about 1M at which the highest yield of specific activity (up to 97%) was obtained. Using the immobilized GroEL column, 3ml of the lysozyme (1mg/ml) per batch could be refolded at an overall yield of 81%, which corresponded to a refolding productivity of 54mg per l gel per h. At comparable reactivation yields (over 80%), this value of productivity was over four-times larger as that of the size-exclusion refolding chromatography reported previously (12mg per l gel perh), indicating the advantage of the present system for producing a high throughput in protein refolding operations.

Crude soybean lecithin was used as a novel surfactant to form reversed micelles in n-hexane. Cibacron Blue F-3GA (CB) was directly immobilized to the reversed micelles by a two-phase reaction. The reversed micellar system without CB showed low solubilizing capacity for low molecular weight proteins, lysozyme, and cytochrome c due to the weak electrostatic interactions. The introduction of CB significantly increased the solubilization of lysozyme because of its affinity binding to CB but showed no effect on the solubilization of cytochrome c since it did not bind to CB. Although bovine serum albumin had an affinity for CB, it was not extracted to the reversed micelles containing CB because its high molecular weight resulted in a significant steric hindrance effect. Thus the reversed micellar system had a high selectivity resulting from both biospecific and steric hindrance effects. The extraction yield of lysozyme decreased significantly with increasing ionic strength. Therefore, the back extraction of lysozyme was carried out using a stripping solution with an ionic strength of 0.865mol/L. The overall recovery yield of lysozyme after back extraction could be increased to 87% by stripping for 2 h. The recovered lysozyme exhibited an activity equivalent to native lysozyme, and its secondary structure was also unchanged.

A predictive model is developed to describe the salt effects on the adsorption equilibrium of protein to Cibacron Blue-modified agarose gel (Sepharose CL-6B). This model assumes that, with the addition of salt, a fraction of dye-ligand molecules will lodge to the surface of the agarose gel resulting from the induced strong hydrophobic interaction between the dye ligands and agarose surface. This leads to a decrease in the dye ligands accessible to protein adsorption and consequently decreases the adsorption capacity of protein. The effect of salt on the dye-ligand lodging is presented by the equilibrium between salt and the dye ligands. Combined with the basic concept of steric-mass action theory, which considers both the multipoint nature and the macromolecule steric shielding of protein adsorption, an implicit isotherm of the protein adsorption equilibrium on Cibacron Blue 3GA-modified Sepharose CL-6B is formulated, involving salt concentration as a variable. Good agreement between experimental data and the predicted adsorption isotherms for single-component protein systems has been demonstrated, and fairly good matching between the predicted and experimental data for the binary adsorption of bovine serum albumin and bovine hemoglobin is obtained under most conditions. This model is expected to be useful in the design and optimization of the salt-gradient elution process of dye-ligand affinity chromatography.

A two-state protein model is proposed to describe the salt effects on protein adsorption equilibrium on hydrophobic media. This model assumes that protein molecules exist in two equilibrium states in a salt solution, that is, hydrated and dehydrated states, and only the dehydrated-state protein can bind to hydrophobic ligands. In terms of the two-state protein hypothesis and the steric mass-action theory, protein adsorption equilibrium on hydrophobic media is formulated by a five-parameter equation. The model is demonstrated with the adsorption of bovine serum albumin to Phenyl Sepharose gels as a model system. The effects of salt type (sodium chloride, sodium sulfate and ammonium sulfate) on the model parameters are discussed. Then, the model formulism is simplified in terms of the small magnitude of the protein dehydration equilibrium constant in the model. This simplification has returned the model derived on the basis of the two-state protein hypothesis to its original mechanism of salt effects on the hydrophobic adsorption of protein. This simplified model also creates satisfactory prediction of protein adsorption isotherms.

A poly(vinyl alcohol)-based magnetic gel entrapping Fe3O4 colloids has been prepared by an emulsification-crosslinking method. The gel was modified with Cibacron blue 3GA, and thus a magnetic affinity support was produced. The adsorption equilibrium studies showed that the adsorption isotherm of lysozyme was nearly rectangular, with a capacity of 254mg/ml, while the adsorption isotherm of bovine serum albumin obeyed the Henry's law. Uptake kinetics of the two proteins was investigated and analyzed with a pore diffusion model and a homogeneous diffusion model. Experimental results showed that the magnetic affinity gel had magnetic responsiveness and favorable properties in protein adsorption, and was mechanically and chemically stable.