Research Article
A methodology for the graphical determination of operating conditions of chromatographic sequences incorporating the trade-offs between purity and yield
Article first published online: 19 OCT 2006
DOI: 10.1002/jctb.1607
Copyright © 2006 Society of Chemical Industry
Issue
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Journal of Chemical Technology and Biotechnology
Volume 81, Issue 11, pages 1803–1813, November 2006
Additional Information
How to Cite
Salisbury, R. S., Bracewell, D. G. and Titchener-Hooker, N. J. (2006), A methodology for the graphical determination of operating conditions of chromatographic sequences incorporating the trade-offs between purity and yield. J. Chem. Technol. Biotechnol., 81: 1803–1813. doi: 10.1002/jctb.1607
Publication History
- Issue published online: 19 OCT 2006
- Article first published online: 19 OCT 2006
- Manuscript Accepted: 21 MAY 2006
- Manuscript Revised: 20 MAY 2006
- Manuscript Received: 3 MAR 2006
- Abstract
- Article
- References
- Cited By
Keywords:
- chromatography;
- windows of operation;
- sequence modelling
Abstract
Multiple-step chromatography sequences are necessary in biopharmaceutical downstream processing to achieve the desired levels of purity for products such as therapeutic proteins. Traditional methods of process design deal with each step individually, but this can result in a sequence that does not achieve best overall performance. This paper proposes a graphical methodology for the identification of operating conditions for a two-step chromatography sequence. The method uses windows of operation to incorporate the trade-offs between yield, purity and productivity. A tie-line procedure is developed that separates the window of operation for the first chromatographic step into two zones. One zone contains those operating conditions that combine to produce a material which can be purified successfully by the second step to produce a product that meets the desired specifications. The second zone consists of operating conditions which will not yield a material that can be adequately purified by a second chromatographic stage to yield a product of the predetermined specifications. The methodology is valuable in that it helps in achieving the rapid design of a two-step chromatography sequence, and aids in choosing the optimum operating conditions for the first step that are highly dependent upon the operation and specifications of the second chromatographic step. Simulations carried out using a software package based on the general rate model depict the construction and use of the method applied to a sequence of ion exchange and hydrophobic interaction chromatography separating a three-component protein mixture. Copyright © 2006 Society of Chemical Industry

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