多级离心连续逆流手性萃取模型及模拟
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  • 英文篇名:Model and simulation on enantioselective separation by continuously countercurrent extraction in a cascade of centrifugal contactor separators
  • 作者:唐课文 ; 张辉 ; 刘永兵 ; 张盼良
  • 英文作者:TANG KeWen1*,ZHANG Hui2,LIU YongBing1,ZHANG PanLiang1 1 Department of Chemistry and Chemical Engineering,Hunan Institute of Science and Technology,Yueyang 414006,China 2 Department of Chemical Engineering,Xiangtan University,Xiangtan 411105,China
  • 关键词:苯基琥珀酸对映体 ; 多级萃取模型 ; 手性萃取 ; 离心萃取器
  • 英文关键词:phenylsuccinic acid enantiomers,multistage extraction model,chiral separation,centrifugal contactor separators
  • 中文刊名:JBXK
  • 英文刊名:Scientia Sinica(Chimica)
  • 机构:湖南理工学院化学化工学院;湘潭大学化工学院;
  • 出版日期:2013-05-20
  • 出版单位:中国科学:化学
  • 年:2013
  • 期:v.43
  • 基金:国家自然科学基金(21176062);; 教育部新世纪优秀人才支持计划;; 湖南省自然科学基金(12JJ2007);; 湖南省高校科技创新团队支持计划;; 湖南省高校重点实验室开放基金(11K029)资助
  • 语种:中文;
  • 页:JBXK201305012
  • 页数:9
  • CN:05
  • ISSN:11-5838/O6
  • 分类号:106-114
摘要
基于单级手性萃取数学模型和质量守恒定律,建立了多级离心手性萃取数学模型,设计了多级离心萃取数学模型程序,并对多级离心萃取分离苯基琥珀酸(PSA)对映体进行了模拟.模拟了相比、萃取剂浓度、对映体浓度、进料位置和萃取级数等工艺参数对萃取效果(产物纯度和产率)的影响.模拟结果表明,考察的工艺参数共同影响萃取相和萃余相的产物纯度及产率;采用中间位置进料和较大的W/F相比有利于对称分离.实验发现:采用中间位置进料,10级离心萃取后萃取相中苯基琥珀酸的光学纯度ee(对映体过量)达到56%以上.模拟结果还表明,采用26级离心萃取器,中间进料,逆流分级萃取,萃取相及萃余相中的光学纯度ee都能达到98%以上.
        Based on a single stage equilibrium model and the law of conservation of mass,a multistage mathematical model of enantioselective liquid-liquid extraction was constructed and programmed in the matlab.The influence of changes in process parameters such as phase ratios,stage,extractant concentration([C]) and racemate concentration([AR,S]),the location of feed,extractant excess and number of stages on ee(enantiomeric excess) and Y(yield) were investigated.The simulation results show that the process parameters have the influence on ee and yield in the extract and the raffinate phase.It is conducive to symmetric separation by use of feeding in the middle stage and the larger phase ratio W/F.The ee of 56% in extract phase was obtained for separation of phenylsuccinic acid enantiomers by feeding in the middle stage in a countercurrent cascade of ten centrifugal contactor separators.A cascade of 26 stages is sufficient for symmetric separation of phenylsuccinic acid enantiomers with 98% equal ee(eeeq) in the extract phase and the raffinate phase.
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