Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/66644
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dc.titleKinetic and equilibrium study of the enantioseparation of Fenoprofen in a batch setup
dc.contributor.authorChing, C.B.
dc.contributor.authorArlt, W.
dc.contributor.authorLisso, M.
dc.contributor.authorWozny, G.
dc.date.accessioned2014-06-17T08:32:46Z
dc.date.available2014-06-17T08:32:46Z
dc.date.issued2000-11
dc.identifier.citationChing, C.B.,Arlt, W.,Lisso, M.,Wozny, G. (2000-11). Kinetic and equilibrium study of the enantioseparation of Fenoprofen in a batch setup. Industrial and Engineering Chemistry Research 39 (11) : 4365-4369. ScholarBank@NUS Repository.
dc.identifier.issn08885885
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/66644
dc.description.abstractThe bed voidage, axial dispersion, and kinetic and isotherm parameters for the chromatographic enantioseparation of racemic Fenoprofen, using cellulose ester as the chiral stationary phase and 2-propanol/hexane/acetyl alcohol as the mobile phase, were evaluated by moment analyses on the basis of equilibrium theory and the linear driving force model. The peak-fitting method was used to identify the coefficients of the competitive Langmuir isotherm for both enantiomers. For this reason and for the validation of the model parameters, a simulation program was developed. The simulated results describe the experimental data well. On the basis of the isotherm parameters and the equilibrium theory, the process region for the simulated moving bed (SMB) process was identified. Changes of the process region will be discussed by considering fluctuations in the feed concentration and uncertainties in the determined capacity factor.
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentCHEMICAL & ENVIRONMENTAL ENGINEERING
dc.description.sourcetitleIndustrial and Engineering Chemistry Research
dc.description.volume39
dc.description.issue11
dc.description.page4365-4369
dc.description.codenIECRE
dc.identifier.isiutNOT_IN_WOS
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