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Measurements and thermodynamic modeling of liquid–liquid equilibria in ternary system 2-methoxy-2-methylpropane+p-cresol+water 被引量:5
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作者 Liejin Luo Dong Liu +1 位作者 Libo Li Yun Chen 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2016年第3期360-364,共5页
Liquid-liquid equilibrium (LLE) data for the ternary system 2-methoxy-2-methylpropane (methyl tert-butyl ether) + p-cresol + water was measured at atmospheric pressure and temperatures of 298.15 K and 313.15 K. ... Liquid-liquid equilibrium (LLE) data for the ternary system 2-methoxy-2-methylpropane (methyl tert-butyl ether) + p-cresol + water was measured at atmospheric pressure and temperatures of 298.15 K and 313.15 K. From the distribution coefficients and selectivity, it was found that 2-methoxy-2-methylpropane is an efficient solvent to extract p-cresol from wastewater. The consistency of the experimental tie-line data was verified with the Hand and Bachman equations. These data were also correlated with the non-random two liquid (NRTL) and universal quasi-chemical correlation activity coefficient (UN1QUAC) models to yield binary interac- tion parameters for p-cresol extraction process evaluation. Both models agreed with experiments very well, yet the NRTL model showed even smaller average deviation than the UNIQUAC model. 展开更多
关键词 Liquid-liquid equilibriaSolvent extractionWaste treatmentnrtluniquacsimulation
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