The selective separation of (S)-amlodipine via a hollow fiber supported liquid membrane: Modeling and experimental verification

被引:41
作者
Sunsandee, Niti [1 ]
Leepipatpiboon, Natchanun [2 ]
Ramakul, Prakorn [3 ]
Pancharoen, Ura [1 ]
机构
[1] Chulalongkorn Univ, Dept Chem Engn, Fac Engn, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Chromatog & Separat Res Unit, Dept Chem, Fac Sci, Bangkok 10330, Thailand
[3] Silpakorn Univ, Dept Chem Engn, Fac Engn & Ind Technol, Nakhon Pathom 73000, Thailand
关键词
Enantiosepartation; HFSLM; O; '-Dibenzoyl-(2S; 3S)-tartaric acid; (S)-Amlodipine; Flux model; ENANTIOSELECTIVE EXTRACTION; CALCIUM-ANTAGONISTS; ENANTIO SEPARATION; SOLVENT-EXTRACTION; MANDELIC-ACID; MASS-TRANSFER; ENANTIOSEPARATION; AMLODIPINE; RESOLUTION; TRANSPORT;
D O I
10.1016/j.cej.2011.11.068
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A hollow fiber supported liquid membrane (HFSLM) containing the chiral selector O,O'-dibenzoyl-(2S,3S)-tartaric acid ((+)-DBTA) was characterized for the enantioseparation of (R,S)-amlodipine. The influence of various chemical parameters, including the concentration of feed and receiving phases, as well as the carrier concentration in the membrane, were also investigated. Valuable knowledge on the transport mechanisms within this system was thus attained. Furthermore, a mathematical model focusing on the extraction side of the liquid membrane system was presented in order to predict the concentration of (S)-amlodipine at different times. The extraction and recovery of (S)-amlodipine from feed phase were 77.50% and 72.50%, respectively. Extraction equilibrium constant (K-ex), distribution ratio (D), permeability (P) and mass transfer coefficients were determined. The aqueous-phase mass-transfer coefficient (k(f)) and organic-phase mass-transfer coefficient (k(m)) were reported to 2.74 x 10(-2) and 2.52 x 10(-2) cm/s, respectively. The results showed promising agreement with the experimental data. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:299 / 308
页数:10
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