Production and purification of TAL6003: a novel version of the protease plasmin.

TAL6003 is an engineered form of human plasmin under development for thrombolytic therapy. TAL6003 (38.2kDa) contains nine disulfide bonds distributed within and between its two functional domains, a 25.2 kDa serine protease domain linked to a 13.0 kDa kringle I domain; kringles 2-5 present in native human plasmin have been deleted from this plasmin molecule. TAL6003 is expressed as its zymogen in Escherichia coli and is harvested in inclusion bodies. Following solubilization of inclusion bodies with urea as the chaotrope and glutathione as the reducing agent, this zymogen is refolded by dilution to a final concentration of 0.5mg/ml, with a yield of 48% (relative to total zymogen). Refolded TAL6003 zymogen is filtered, diafiltered, and filtered again prior to capture and purification on SP Sepharose, which is highly effective in removing host-cell protein. Subsequent affinity purification on ECH-Lysine Sepharose serves to capture polypeptide chains containing correctly refolded kringle 1 domain, which is the locus of the molecule's lysine-binding site, and to further eliminate host-cell protein. TAL6003 zymogen eluted from the ECH-Lysine Sepharose column is activated to TAL6003 with streptokinase, with an activity yield of approximately 80%. Proteolytically active TAL6003 is stripped of streptokinase by passage through an anion-exchange (Q) membrane and is then affinity purified on Benzamidine Sepharose, which serves to remove unreacted TAL6003 zymogen and proteolytically degraded TAL6003. An ultrafiltration/diafiltration step, to concentrate and to formulate TAL6003, completes the purification process. The final product exhibited a specific activity of close to unity and high purity by several relevant criteria.

Purification of recombinant DNA-derived factor IX produced in transgenic pig milk and fractionation of active and inactive subpopulations.

Transgenic animal bioreactors can be engineered to make gram per liter quantities of complex recombinant glycoproteins in milk. However, little is known about the limitations in post-translational processing that occurs for very complex proteins and how this impacts the task of purification. We report on the purification of recombinant factor IX (rFIX) from the milk of transgenic pigs having an expression level of 2-3 g rFIX/(l(-1) h(-1)), an expression level that is about 20-fold higher than previously reported. This purification process efficiently recovers highly active rFIX and shows that even complex mixtures like pig milk, which contains 60 g/l total endogenous milk protein and multiple subpopulations of rFIX, can be processed using conventional, non-immunoaffinity chromatographic methods. Without prior removal of caseins, heparin-affinity chromatography was used to first purify the total population of rFIX at greater than 90% yield. After the total population was isolated, the biologically active and inactive subpopulations were fractionated by high-resolution anion exchange chromatography using an ammonium acetate elution. Capillary isoelectric focusing of the active and inactive rFIX fractions demonstrated that the active subpopulations are the most acidic.