Bioseparations and Downstream Processing
Process and economic evaluation for monoclonal antibody purification using a membrane-only process
Article first published online: 26 MAY 2011
DOI: 10.1002/btpr.639
Copyright © 2011 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Varadaraju, H., Schneiderman, S., Zhang, L., Fong, H. and Menkhaus, T. J. (2011), Process and economic evaluation for monoclonal antibody purification using a membrane-only process. Biotechnol Progress, 27: 1297–1305. doi: 10.1002/btpr.639
Publication History
- Issue published online: 10 OCT 2011
- Article first published online: 26 MAY 2011
- Accepted manuscript online: 2 MAY 2011 07:01AM EST
- Manuscript Revised: 15 APR 2011
- Manuscript Received: 8 FEB 2011
Funded by
- Chemical and Biological Separations (CBS) Program in the Chemmical, Bioengineering, Environmental, and Transport Systems (CBET) Division of the National Science Foundation (NSF). Grant Number: CBET-0827844
- Department of Chemical and Biological Engineering at the South Dakota School of Mines and Technology
- Abstract
- Article
- References
- Cited By
Keywords:
- membrane adsorption;
- electrospun nanofibers;
- monoclonal antibody production;
- process economics
Abstract
In recent years, the market for therapeutic monoclonal antibodies (mAb) has grown exponentially, and with this there has been a desire to reduce the costs associated with production and purification of these high-value biological products. A typical mAb purification process involves three adsorption/chromatography steps [protein A, ion exchange (IEX), and hydrophobic interaction (HIC)], along with ultrafiltration, nanofiltration, and microfiltration. With the development of membrane adsorption/chromatography as a viable alternative to traditional pack bed systems, the opportunity exists to complete the entire downstream purification process using only membrane operations. In this study, the process simulation tool SuperPro Designer was used to evaluate the application of recently developed ultra-high capacity electrospun nanofibrous adsorption membranes as a replacement for conventional chromatographic media in the downstream mAb production process. The simulation showed that nanofibrous adsorption membranes in place of the three packed bed chromatography steps reduced the required volume of protein A, IEX, and HIC adsorptive medium by 25, 80, and 80%, respectively. In addition, the membrane-only process reduced the downstream processing time by 50%, decreased the number of labor hours associated with the purification steps by 40%, generated 40% less aqueous waste, and reduced the overall downstream process operating expenses per unit product by 23%. There were also significant savings in facility construction costs and the price of fixed equipment required for separations. With these savings not only is the membrane-only process economically competitive with the traditional packed bed operations, but it offers the possibility of moving toward more disposable process.© 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011

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