Bioseparations and Downstream Processing
Liquid–liquid extraction for recovery of paclitaxel from plant cell culture: Solvent evaluation and use of extractants for partitioning and selectivity
Article first published online: 18 JUN 2012
DOI: 10.1002/btpr.1562
Copyright © 2012 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
McPartland, T. J., Patil, R. A., Malone, M. F. and Roberts, S. C. (2012), Liquid–liquid extraction for recovery of paclitaxel from plant cell culture: Solvent evaluation and use of extractants for partitioning and selectivity. Biotechnol Progress, 28: 990–997. doi: 10.1002/btpr.1562
Publication History
- Issue published online: 7 AUG 2012
- Article first published online: 18 JUN 2012
- Accepted manuscript online: 11 MAY 2012 10:08AM EST
- Manuscript Revised: 26 APR 2012
- Manuscript Received: 9 MAR 2012
Funded by
- University of Massachusetts Center for Process Design and Control
- E.I. Dupont Co.
- National Science Foundation. Grant Number: CBET9984463
- National Institutes of Health. Grant Number: GM070852
- Abstract
- Article
- References
- Cited By
Keywords:
- plant cell culture;
- paclitaxel;
- bioseparations;
- downstream processing;
- partition coefficient;
- selectivity
Abstract
A major challenge in the production of metabolites by plant cells is the separation and purification of a desired product from a number of impurities. An important application of plant cell culture is the biosynthesis of the anticancer agent paclitaxel. Liquid–liquid extraction plays a critical role in the recovery of paclitaxel and other valuable plant-derived products from culture broth. In this study, the extraction of paclitaxel and a major unwanted by-product, cephalomannine, from plant cell culture broth into organic solvents is quantified. Potential solvent mixtures show varying affinity and selectivity for paclitaxel over cephalomannine. The partition coefficient of paclitaxel is highest in ethyl acetate and dichloromethane, with measured values of 28 and 25, respectively; however, selectivity coefficients are less than 1 for paclitaxel over cephalomannine for both solvents. Selectivity coefficient increases to 1.7 with extraction in n-hexane, but the partition coefficient decreases to 1.9. Altering the pH of the aqueous phase results in an increase in both recovery and selectivity using n-hexane but does not change the results for other solvents significantly. The addition of extractants trioctylamine (TOA) or tributylphosphate (TBP) to n-hexane gives significantly higher partition coefficients for paclitaxel (8.6 and 23.7, respectively) but no selectivity. Interestingly, when 20% hexafluorobenzene (HFB) is added to n-hexane, the partition coefficient remains approximately constant, but the selectivity coefficient for paclitaxel over cephalomannine improves to 4.5. This significant increase in selectivity early in the purification process has the potential to simplify downstream processing steps and significantly reduce overall purification costs. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 990–997, 2012

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