Adsorption of plasmid DNA on ceramic hydroxyapatite chromatographic materials.

The adsorption of plasmid DNA onto two different types of ceramic hydroxyapatite beads with a particle diameter of 20 µm, namely Ceramic Hydroxyapatite Type II and the Type III, which is not commercially available, were investigated. Type II and the Type III have a pore diameter of 80 and 240 nm, respectively. Equilibrium and dynamic binding capacity for a 4.9 kbp model plasmid on Ceramic Hydroxyapatite Type II and Type III were enhanced by addition of NaCl to the adsorption buffer. This result indicates that the adsorption mechanism cannot be solely explained by electrostatic interaction. The affinities of plasmid DNA for Ceramic Hydroxyapatite Type II (with a K(D) of ≈0.005 mg/mL) and to Hydroxyapatite Type III (with a K(D) of ≈0.045 mg/mL) were not affected by NaCl, whereas the binding capacity was. This observation corroborates the assumption that a change of the shape of the plasmid molecule is affected and could be the reason for increased binding capacity with salt. The maximal binding capacity shows that at least a part of the CHT II bead must be accessible for the plasmid, whereas CHT III can be saturated with the plasmid. In both cases, an extremely hindered transport takes place.

Matrix-assisted refolding of autoprotease fusion proteins on an ion exchange column: a kinetic investigation.

Matrix-assisted refolding is an excellent technique for performing refolding of recombinant proteins at high concentration because aggregation during refolding is partially suppressed. The autoprotease N(pro) and its engineered mutant EDDIE can be efficiently refolded on cation-exchangers. In the current work, denatured fusion proteins were loaded at different column saturations (5 and 50 mg mL(-1) gel), and refolding and self-cleavage were initiated during elution. The contact time of the protein with the matrix significantly influenced the refolding rate and yield. On POROS 50 HS, the refolding rate was comparable to a batch refolding process, but yield was substantially higher; at a protein concentration of 1.55 mg mL(-1), an almost complete conversion was observed. With Capto S, the rate of self-cleavage increased by a factor of 20 while yield was slightly reduced. Processing the autoprotease fusion protein on Capto S at a high protein loading of 50 mg mL(-1) gel and short contact time (0.5h) yielded the highest productivity.

Matrix-assisted refolding of autoprotease fusion proteins on an ion exchange column.

Refolding of proteins must be performed under very dilute conditions to overcome the competing aggregation reaction, which has a high reaction order. Refolding on a chromatography column partially prevents formation of the intermediate form prone to aggregation. A chromatographic refolding procedure was developed using an autoprotease fusion protein with the mutant EDDIE from the N(pro) autoprotease of pestivirus. Upon refolding, self-cleavage generates a target peptide with an authentic N-terminus. The refolding process was developed using the basic 1.8-kDa peptide sSNEVi-C fused to the autoprotease EDDIE or the acidic peptide pep6His, applying cation and anion exchange chromatography, respectively. Dissolved inclusion bodies were loaded on cation exchange chromatographic resins (Capto S, POROS HS, Fractogel EMD SO(3)(-), UNOsphere S, SP Sepharose FF, CM Sepharose FF, S Ceramic HyperD F, Toyopearl SP-650, and Toyopearl MegaCap II SP-550EC). A conditioning step was introduced in order to reduce the urea concentration prior to the refolding step. Refolding was initiated by applying an elution buffer containing a high concentration of Tris-HCl plus common refolding additives. The actual refolding process occurred concurrently with the elution step and was completed in the collected fraction. With Capto S, POROS HS, and Fractogel SO(3)(-), refolding could be performed at column loadings of 50mg fusion protein/ml gel, resulting in a final eluate concentration of around 10-15 mg/ml, with refolding and cleavage step yields of around 75%. The overall yield of recovered peptide reached 50%. Similar yields were obtained using the anion exchange system and the pep6His fusion peptide. This chromatographic refolding process allows processing of fusion peptides at a concentration range 10- to 100-fold higher than that observed for common refolding systems.