Title of article :
Chiral separation by combining pertraction and preferential crystallization
Author/Authors :
Robl، نويسنده , , S. and Gou، نويسنده , , L. and Gere، نويسنده , , A. and Sordo، نويسنده , , M. and Lorenz، نويسنده , , H. A. Mayer، نويسنده , , A. and Pauls، نويسنده , , C. and Leonhard، نويسنده , , K. and Bardow، نويسنده , , A. and Seidel-Morgenstern، نويسنده , , A. and Schaber، نويسنده , , K.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2013
Pages :
9
From page :
80
To page :
88
Abstract :
This work describes the application of a hybrid two-step enantioselective separation process. As a first step, pertraction using supported liquid membranes provides an initial enrichment, while the following preferential crystallization delivers the enantiopure crystals as final product. Mandelic acid in water was studied as a model system. Using a suitable chiral selector, pertraction provides enrichments exceeding 10% and reaching up to 20% in the permeate phase, which was sufficient to allow for subsequent selective preferential crystallization. Based on the individual performances of pertraction and crystallization, overall yields and productivities are estimated. The calculated productivities are compared with values achievable in alternatively applicable chromatographic separation processes using chiral stationary phases. The realized hybrid pertraction-crystallization process is in its present state for the example considered still inferior to preparative chromatography. Strategies for further improvement are suggested.
Keywords :
Pertraction , Liquid membrane , Preferential crystallization , Hybrid process , Productivity , Enantiomers
Journal title :
Chemical Engineering and Processing: Process Intensification
Serial Year :
2013
Journal title :
Chemical Engineering and Processing: Process Intensification
Record number :
1611127
Link To Document :
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