Chemistry: molecular biology and microbiology – Micro-organism – tissue cell culture or enzyme using process... – Using a micro-organism to make a protein or polypeptide
Patent
1996-11-22
2000-08-15
Naff, David M.
Chemistry: molecular biology and microbiology
Micro-organism, tissue cell culture or enzyme using process...
Using a micro-organism to make a protein or polypeptide
435 41, 435 691, 435 692, 435814, 530414, C12P 2104, C12P 2106, C12P 100, C07K 134
Patent
active
061035025
ABSTRACT:
A peptide such as in a cell-free fermentation medium is ultrafiltered with a membrane having a molecular weight cut-off of at least approximately two times greater than the molecular weight of the peptide. The peptide is retained by the membrane, and is desalinated and concentrated to provide prepurification of the peptide. A preferred temperature for ultrafiltration is about 5 to about 15.degree. C. Permeate flow rate may be about 10 l/m.sup.2 /h to about 35 l/m.sup.2 /h, and permeate conductivity may be less than about 10 mS/cm. The permeate may be recycled until peptide concentration is constant. A cell-free fermentation medium containing hirudin from a recombinant microorganism such as Saccharomyces cerevisiae is ultrafiltered with a membrane having a molecular weight cut-off of about 20 kD to about 30 kD.
REFERENCES:
patent: 5180668 (1993-01-01), Crause et al.
patent: 5422249 (1995-06-01), Liersch et al.
patent: 5468844 (1995-11-01), Smith
patent: 5616476 (1997-04-01), Crause et al.
Scott K., Handbook of Industrial Membranes, 1995 Elsevier Science Publishers LTD., pp. 32-33.
Brockelbank, et al., "Primary Separation" Chap. 4in G. Schmidt-Kastner et al., Hsg.: "Recovery of Bioproducts", European Federation of Biotechnology, Study Report of Working Party on Downstream Processing, 1993, pp. 1-130.
Eriksson, Desalination, 53:259-263 (1985), "Some Examples Of The Use of Crossflow Filtration In The Downstream Processing In A Biochemical Industry".
Winzeler, Chimia, 44:288-291 (1990), "Membran-Filtration mit hoher Trennleistung und minimalem Energiebedarf" (In German).
Muller et al., Chem. Ing.-Tech. 62:(5):380-390 (1990), "Die Chromatographie, eine zentrale Methode in der biotechnischen Aufarbeitung" (In German).
Sullivan et al., Chem. Eng. Prog. 80(1):68-75 (1984), Use of this membrane separation technique will accelerate because of its economic and processing advantages and the availability of new membrane materials.
Flaschel et al., Adv. In Biochem. Engineering/Biotechnology, vol. 26, Downstream Processing, S. 73-142, N.Y. (1983); Ed.: D.J. Bell.
Atkinson et al., Biochem. Engineering and Biotechnology Handbook, Chap. 16, "Downstream Processing" and Chap. 17m "Product Recovery Processes and Unit Operations", Second Ed., Stockton Press 1991, New York.
Dodt et al., Biol. Chem. Hoppe-Seyler, 366:379-385 (1985), "The Complete Covalent Structure of Hirudin".
Markwardt, Biomed. Biochem. Acta, 44:1007-1013 (1985), "Pharmacology of Hirudin: One hundred years after the first report of the anticoagulant agent in medicinal leeches".
Moller Jorg
Richard Frank
Aventis Pharma Deutschland GmbH
Naff David M.
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