Experiments and correlations of phase equilibria of ethanol-ethyl acetate-water ternary mixture.

Isobaric (vapour+liquid+liquid) equilibrium data for (di-n-propyl ether+n-propyl alcohol+water) and (diisopropyl ether+isopropyl alcohol+water) systems at 100kPa

“…Although the calculated ternary VLLE did not always agree with the experimental data. There are some studies [2,3] that concluded that the isobaric VLLE was better estimated by the parameters from the ternary LLE than those from the binary VLE data. On the other hand, other papers [4] reported that the isobaric VLLE was well estimated by the parameters determined from the binary VLE data.…”

Enhancement of liquid phase splitting of water + ethanol + ethyl acetate mixtures in the presence of a hydrophilic agent or an electrolyte substance

“…The Electrolyte-NRTL model reduces to the original NRTL model [21] for salt-free systems. [4] Water + ethyl acetate VLE Pai and Rao [1] Rajendran et al [5] Ethanol + ethyl acetate VLE Kato et al [6] Lee et al [7] Nagata et al [8] Ortega et al [9] Tochigi et al [10] Tu et al [11] Yan et al [12] Water + KAc VLE Zemp and Francesconi [13] Water …”

Phase equilibria for reactive distillation of diethyl succinate. Part II: Systems diethyl succinate+ethyl acetate+water and diethyl succinate+acetic acid+water

“…Values for q and the relative volume r were taken from the Aspen database. Due to the modification of q for H 2 O and EtOH, interaction parameters for the binaries H 2 O + AcAc, H 2 O + EtAc, EtOH + AcAc, and EtOH + EtAc were regressed using VLE and LLE data reported in literature [37][38][39][40][41][42][43][44][45][46]. Interaction parameters for the binaries H 2 O + EtOH, H 2 O + DES, and EtOH + DES were obtained before for the UNI-QUAC equation.…”

“…6-8. [39], ( ) Lee [41], (×) Ellis data in [44], (᭹) Kato [47], and (-) UNIQUAC-HOC. VLE experimental data for the system EtOH + EtAc agree with those reported before as shown in Fig.…”