4 research outputs found
Estudio del equilibrio lĂquido-lĂquido de benceno + (hexano, heptano y ciclohexano) con el lĂquido iĂłnico 1-etil-3-metilimidazolio etilsulfato a 308,15 k
Get PDFSe determinĂł el equilibrio lĂquido-lĂquido(ELL) de los sistemas ternarios benceno+ (hexano, heptano y ciclohexano)con el lĂquido iĂłnico 1-etil-3-metilimidazolioetilsulfato (EMIM-EtSO4) a 308,15K; la selectividad (S) y el coeficiente dedistribuciĂłn (β) se calcularon desde losdatos experimentales que se utilizaronpara determinar la capacidad del lĂquidoiĂłnico como solvente para la separaciĂłndel aromático desde sus mezclas con hidrocarburosalifáticos. La regiĂłn de inmiscibilidadaumentĂł en el siguiente orden:ciclohexano and lt; hexano and lt; heptano. Laconsistencia de los datos experimentalesdel ELL es evaluado usando la ecuaciĂłnde Othmer-Tobias. La composiciĂłn delas fases en equilibrio se correlacionĂłcon los modelos para coeficientes de actividadNRTL y Uniquac
Estudio del equilibrio lĂquido-lĂquido de tolueno + heptano con el lĂquido iĂłnico 1,3-dimetilimidazolio metilsulfato a 318.15 K
Get PDFThe extraction of toluene from heptane was analyzedby liquid extraction with 1,3-dimethylimidazolium methylsulfate[MMim][MeSO4] ionic liquid, as a solvent.The experimental (liquid + liquid) equilibrium (LLE)data were determined at T= 318.15 K and atmosphericpressure. Selectivity and distribution coefficient,derived from the tie-lines, were used to determine theability of this ionic liquid as solvent for the separationof toluene from its mixtures with heptane. Thedegree of consistency of the experimental LLE datawas ascertained using the Othmer–Tobias equation.The experimental data for LLE of the ternary systemwere correlated with the Non-Random Two-Liquid(NRTL) and UNIversal QUAsi-Chemical (UNIQUAC)thermodynamic models
Estudio del equilibrio lĂquido-lĂquido de tolueno + heptano con el lĂquido iĂłnico 1,3-dimetilimidazolio metilsulfato a 318.15 K
Get PDFThe extraction of toluene from heptane was analyzedby liquid extraction with 1,3-dimethylimidazolium methylsulfate[MMim][MeSO4] ionic liquid, as a solvent.The experimental (liquid + liquid) equilibrium (LLE)data were determined at T= 318.15 K and atmosphericpressure. Selectivity and distribution coefficient,derived from the tie-lines, were used to determine theability of this ionic liquid as solvent for the separationof toluene from its mixtures with heptane. Thedegree of consistency of the experimental LLE datawas ascertained using the Othmer–Tobias equation.The experimental data for LLE of the ternary systemwere correlated with the Non-Random Two-Liquid(NRTL) and UNIversal QUAsi-Chemical (UNIQUAC)thermodynamic models
Estudio del equilibrio lĂquido-lĂquido de tolueno + heptano con el lĂquido iĂłnico 1,3-dimetilimidazolio metilsulfato a 318.15 K
No full textThe extraction of toluene from heptane was analyzedby liquid extraction with 1,3-dimethylimidazolium methylsulfate[MMim][MeSO4] ionic liquid, as a solvent.The experimental (liquid + liquid) equilibrium (LLE)data were determined at T= 318.15 K and atmosphericpressure. Selectivity and distribution coefficient,derived from the tie-lines, were used to determine theability of this ionic liquid as solvent for the separationof toluene from its mixtures with heptane. Thedegree of consistency of the experimental LLE datawas ascertained using the Othmer–Tobias equation.The experimental data for LLE of the ternary systemwere correlated with the Non-Random Two-Liquid(NRTL) and UNIversal QUAsi-Chemical (UNIQUAC)thermodynamic models
