Mathematical modeling of penicillin G extraction in an emulsion liquid membrane system containing only a surfactant in the membrane phase
- Authors
- Lee, SC; Chang, JH; Ahn, BS; Lee, WK
- Issue Date
- 1998-10-14
- Publisher
- ELSEVIER SCIENCE BV
- Citation
- JOURNAL OF MEMBRANE SCIENCE, v.149, no.1, pp.39 - 49
- Abstract
- An extraction experiment of penicillin G was performed in an emulsion liquid membrane system in which only ECA 4360J exists in the organic membrane phase without a predominant carrier, Amberlite LA-2, used in our previous works and it functions as a carrier as well as a surfactant. A permeation model for the present system has been developed as a primary study to examine the transport mechanism of penicillin G in the previous batch and continuous systems with two carriers of Amberlite LA-2 and ECA 4360J. The model takes into account the mass transfer in the external aqueous film, the extraction reaction between penicillin G and ECA 4360J at the external interface, the diffusion of penicillin G in the emulsion phase, the stripping reaction at the internal interface and the pH change of internal aqueous solution containing Na2CO3 with penicillin G transported into the internal phase. The experimental data were well fitted with the present model. Also, an expression for the reaction of penicillin G with ECA 4360J was obtained through a series of equilibrium measurements in liquid-liquid extraction system. (C) 1998 Published by Elsevier Science B.V. All rights reserved.
- Keywords
- MASS-TRANSFER; MASS-TRANSFER; emulsion liquid membrane; penicillin G extraction; permeation model; extraction equilibrium
- ISSN
- 0376-7388
- URI
- https://pubs.kist.re.kr/handle/201004/142798
- Appears in Collections:
- KIST Article > Others
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