Scale-up of the Solid−Liquid Extraction Using Characteristic Function Technique

A scale-up methodology based on the characteristic function approximation for the mass-transfer rate is proposed that provides a reliable and inexpensive method for designing and controlling an extraction apparatus. The characteristic function is derived in terms of the usual kinetic and equilibrium...

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Bibliographic Details
Published inIndustrial & engineering chemistry research Vol. 43; no. 16; pp. 4903 - 4907
Main Authors Simeonov, E, Seikova, I, Pentchev, I, Mintchev, A
Format Journal Article
LanguageEnglish
Published Washington, DC American Chemical Society 04.08.2004
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Summary:A scale-up methodology based on the characteristic function approximation for the mass-transfer rate is proposed that provides a reliable and inexpensive method for designing and controlling an extraction apparatus. The characteristic function is derived in terms of the usual kinetic and equilibrium parameters. An analytical expression for the overall resistance to mass transfer is also obtained, providing a linearly variable mass-transfer resistance during the extraction. Experimental data for the kinetics of extraction in a laboratory-scale batch extractor from four solid−liquid systems are presented and discussed in relation to the theory. The calculation procedure is applied to estimate the extraction times in a continuous-action apparatus corresponding to an assigned extraction yield. The calculation results are also supported by experiments in a pilot screw extractor.
Bibliography:ark:/67375/TPS-B0RTXFPS-Z
istex:5482A47EA0293A264D007FD70B74642B03423821
ISSN:0888-5885
1520-5045
DOI:10.1021/ie030650m