Novel multimodal cation-exchange membrane for the purification of a single-chain variable fragment from Pichia pastoris supernatant.

A novel salt-tolerant cation-exchange membrane, prepared with a multimodal ligand, 2-mercaptopyridine-3-carboxylic acid (MMC-MPCA), was examined for its purification properties in a bind-and-elute mode from the high conductivity supernatant of a Pichia pastoris fermentation producing and secreting a single-chain variable fragment (scFv). If successful, this approach would eliminate the need for a buffer exchange prior to product capture by ion-exchange. Two fed-batch fermentations of Pichia pastoris resulted in fermentation supernatants reaching an scFv titer of 395.0 mg/L and 555.7 mg/L, both with a purity of approximately 83 %. The MMC-MPCA membrane performance was characterized in terms of pH, residence time (RT), scFv load, and scFv concentration to identify the resulting dynamic binding capacity (DBC), yield, and purity achieved under optimal conditions. The MMC-MPCA membrane exhibited the highest DBC of 39.06 mg/mL at pH 5.5, with a residence time of 1 min, while reducing the pH below 5.0 resulted in a significant decrease of the DBC to around 2.5 mg/mL. With almost no diffusional limitations, reducing the RT from 2 to 0.2 min did not negatively impact the DBC of the MMC-MPCA membrane, resulting in a significant improvement in productivity of up to 180 mg/mL/min at 0.2 min RT. Membrane fouling was observed when reusing the membranes at 0.2 and 0.5 min RT, likely due to the enhanced adsorption of impurities on the membrane. Changing the amount of scFv loaded onto the membrane column did not show any changes in yield, instead a 10-20 % loss of scFv was observed, which suggested that some of the produced scFv were fragmented or had aggregated. When performing the purification under the optimized conditions, the resulting purity of the product improved from 83 % to approximately 92-95 %.

A novel approach for production of an active N-terminally truncated Ulp1 (SUMO protease 1) catalytic domain from Escherichia coli inclusion bodies.

The SUMO fusion system is widely used to facilitate recombinant expression and production of difficult-to-express proteins. After purification of the recombinant fusion protein, removal of the SUMO-tag is accomplished by the yeast cysteine protease, SUMO protease 1 (Ulp1), which specifically recognizes the tertiary fold of the SUMO domain. At present, the expression of the catalytic domain, residues 403-621, is used for obtaining soluble and biologically active Ulp1. However, we have observed that the soluble and catalytically active Ulp1403-621 inhibits the growth of E. coli host cells. In the current study, we demonstrate an alternative route for producing active Ulp1 catalytic domain from a His-tagged N-terminally truncated variant, residues 416-621, which is expressed in E. coli inclusion bodies and subsequently refolded. Expressing the insoluble Ulp1416-621 variant is advantageous for achieving higher production yields. Approximately 285 mg of recombinant Ulp1416-621 was recovered from inclusion bodies isolated from 1 L of high cell-density E. coli batch fermentation culture. After Ni2+-affinity purification of inactive and denatured Ulp1416-621 in 7.5 M urea, different refolding conditions with varying l-arginine concentration, pH, and temperature were tested. We have successfully refolded the enzyme in 0.25 M l-arginine and 0.5 M Tris-HCl (pH 7) at room temperature. Approximately 80 mg of active Ulp1416-621 catalytic domain can be produced from 1 L of high cell-density E. coli culture. We discuss the applicability of inclusion body-directed expression and considerations for obtaining high expression yields and efficient refolding conditions to reconstitute the active protein fold.