Abstract
Lactic acid is an important commercial product and extracting this from aqueous solution is a growing requirement in fermentation-based industries. The design of an amine extraction process requires (i) equilibrium and (ii) kinetic data for the acid-amine (solvent) system used. The equilibrium complexation constants for ratios of (1:1) and (2:1) have been estimated. The kinetics of extraction of lactic acid by Alamine 336 in decanol has also been determined. The reaction between lactic acid and Alamine 336 in decanol in a stirred cell falls in Regime 3, ie extraction accompanied by a fast chemical reaction occurring in the diffusion film. The reaction has been found to be zero order in Alamine 336 and first order in lactic acid with a rate constant of 0.21 s-1. These data will be useful in the design of extraction processes.
Original language | Undefined |
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Pages (from-to) | 1-8 |
Number of pages | 8 |
Journal | Journal of chemical technology and biotechnology |
Volume | 77 |
Issue number | 9 |
DOIs | |
Publication status | Published - 2002 |
Keywords
- Kinetics
- Reactive extraction
- Equilibria
- METIS-210785
- Lactic acid
- Alamine 336
- decanol
- IR-71847