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Very Large Scale Monoclonal Antibody Purification: The Case for Conventional Unit Operations
Author(s) -
Kelley Brian
Publication year - 2007
Publication title -
biotechnology progress
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.572
H-Index - 129
eISSN - 1520-6033
pISSN - 8756-7938
DOI - 10.1021/bp070117s
Subject(s) - ultrafiltration (renal) , downstream processing , monoclonal antibody , filtration (mathematics) , cross flow filtration , diafiltration , process development , limiting , recombinant dna , process engineering , chromatography , production (economics) , scale (ratio) , process (computing) , unit operation , size exclusion chromatography , biochemical engineering , computer science , chemistry , antibody , membrane , engineering , microfiltration , mathematics , biology , chemical engineering , biochemistry , macroeconomics , enzyme , operating system , quantum mechanics , immunology , mechanical engineering , statistics , physics , economics , gene
Abstract Technology development initiatives targeted for monoclonal antibody purification may be motivated by manufacturing limitations and are often aimed at solving current and future process bottlenecks. A subject under debate in many biotechnology companies is whether conventional unit operations such as chromatography will eventually become limiting for the production of recombinant protein therapeutics. An evaluation of the potential limitations of process chromatography and filtration using todayapos;s commercially available resins and membranes was conducted for a conceptual process scaled to produce 10 tons of monoclonal antibody per year from a single manufacturing plant, a scale representing one of the worldapos;s largest single‐plant capacities for cGMP protein production. The process employs a simple, efficient purification train using only two chromatographic and two ultrafiltration steps, modeled after a platform antibody purification train that has generated 10 kg batches in clinical production. Based on analyses of cost of goods and the production capacity of this very large scale purification process, it is unlikely that non‐conventional downstream unit operations would be needed to replace conventional chromatographic and filtration separation steps, at least for recombinant antibodies.

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