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Continuous chiral separation of 2-phenylbutyric acid by liquid-liquid extraction in centrifugal contactor separators
被引:19
|作者:
Xu, Weifeng
[1
]
Dai, Guilin
[1
]
Tang, Kewen
[1
]
Zhang, Panliang
[1
]
Xiong, Biquan
[1
]
Liu, Yu
[1
]
机构:
[1] Hunan Inst Sci & Technol, Dept Chem & Chem Engn, Yueyang 414006, Hunan, Peoples R China
关键词:
Multistage equilibrium model;
Simulation;
Optimization;
Enantioselective liquid-liquid extraction;
2-phenylbutyric acid;
MOVING-BED CHROMATOGRAPHY;
MEMBRANE TECHNOLOGY;
ENANTIOMERS;
OPTIMIZATION;
D O I:
10.1016/j.seppur.2017.01.063
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
The continuous enantioselective liquid-liquid extraction of 2-phenylbutyric acid (2-PBA) enantiomers by hydroxyethyl-p-cyclodextrin (HE -beta-CD) in aqueous phase using centrifugal contactor separators (CCSs) was studied. Purity (enantiomeric excess, ee) and yield (Y) were used to evaluate the process performance. A multistage equilibrium model was established on the basis of single-stage model for chiral extraction of 2-PBA enantiomers and the law of mass conservation. To verify the model, factors that influencing purity and yield were studied, such as rotational speed of CCSs, volume ratio of extract phase to wash phase (W/O), volume ratio of extract phase to feed phase (W/F), extractant concentration, pH value and number of stages. Results indicated that model predictions were in good accordance with experimental results. The model was applied to predict and optimize the symmetrical separation of 2-PBA enantiomers. The optimal condition was obtained as follows, rotational speed of 3000 rpm, W/O of 4.0, pH of 3.00 and HE-beta-CD concentration of 0.05 mol/L, where equal enantiomeric excess (ee(eq)) can reach up to 42%. The simulated results by the model reveal that the minimum number of stages for eeeq > 97% and eeeq > 99% is 60 and 82, respectively. (C) 2017 Elsevier B.V. All rights reserved.
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页码:53 / 60
页数:8
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