High quality human immunoglobulin G purified from Cohn fractions by liquid chromatography

In order to obtain intravenous immunoglobulin G (iv IgG) of high quality from F-I+II+III or F-II+III pastes prepared by the Cohn method, we developed a chromatography process using ion exchange gels, Q-Sepharose FF and CM-Sepharose FF, and Sephacryl S-300 gel filtration. Viral inactivation was performed by incubating the preparation with pepsin at pH 4.0 at 35oC for 18 h. The characteristics of 28 batches produced by us were: yield 4.3 + or - 0.2 g/l plasma, i.e., a recovery of 39.1 + or - 1.8 percent; IgG subclasses distribution: IgG1 = 58.4 percent, IgG2 = 34.8 percent, IgG3 = 4.5 percent and IgG4 = 2.3 percent; IgG size distribution was 98.4 percent monomers, 1.2 percent dimers and 0.4 percent polymers and protein aggregates; anticomplement activity was less than 0.5 CH50/mg IgG, and prekallikrein activator activity (PKA) was less than 5 IU/ml. These characteristics satisfied the requirements of the European Pharmacopoea edition, and the regulations of the Brazilian Health Ministry (M.S. Portaria No. 2, 30/10/1998)

A chromatographic method for the production of a human immunoglobulin G solution for intravenous use

Immunoglobulin G (IgG) of excellent quality for intravenous use was obtained from the cryosupernatant of human plasma by a chromatographic method based on a mixture of ion-exchange, DEAE-Sepharose FF and arginine Sepharose 4B affinity chromatography and a final purification step by Sephacryl S-300 HR gel filtration. The yield of 10 experimental batches produced was 3.5 g IgG per liter of plasma. A solvent/detergent combination of 1 per cent Tri (n-butyl) phosphate and 1 per cent Triton X-100 was used to inactivate lipid-coated viruses. Analysis of the final product (5 per cent liquid IgG) based on the mean for 10 batches showed 94 per cent monomers, 5.5 per cent dimers and 0.5 per cent polymers and aggregates. Anticomplementary activity was 0.3 CH50/mg IgG and prekallikrein activator levels were less than 5 IU/ml. Stability at 37oC for 30 days in the liquid state was satisfactory. IgG was stored in flasks (2.5 g/flask) at 4 to 8oC. All the characteristics of the product were consistent with the requirements of the 1997 Pharmacopée Européenne.

Purification of human albumin by the combination of the method of Cohn with liquid chromatography

Large volumes of plasma can be fractionated by the method of Cohn at low cost. However, liquid chromatography is superior in terms of the quality of the product obtained. In order to combine the advantages of each method, we developed an integrated method for the production of human albumin and immunoglobulin G (IgG). The cryoprecipitate was first removed from plasma for the production of factor VIII and the supernatant of the cryoprecipitate was fractionated by the method of Cohn. The first precipitate, containing fractions (F)-I + II + III, was used for the production of IgG by the chromatographic method (see Tanaka K et al. (1998) Brazilian Journal of Medical and Biological Research, 31: 1375-1381). The supernatant of F-I + II + III was submitted to a second precipitation and F-IV was obtained and discarded. Albumin was obtained from the supernatant of the precipitate F-IV by liquid chromatography, ion-exchange on DEAE-Sepharose FF, filtration through Sephacryl S-200 HR and introduction of heat treatment for fatty acid precipitation. Viral inactivation was performed by pasteurization at 60oC for 10 h. The albumin product obtained by the proposed procedure was more than 99 per cent pure for the 15 lots of albumin produced, with a mean yield of 25.0 ñ 0.5 g/l plasma, containing 99.0 to 99.3 per cent monomer, 0.7 to 1.0 per cent dimers, and no polymers. Prekallikrein activator levels were ó5 IUml. This product satisfies the requirements of the 1997 Pharmacopée Européenne.