Vapor-liquid equilibria at 453.25 K and excess enthalpies at 363.15 K and 413.15 K for mixtures of benzene, toluene, phenol, benzaldehyde, and benzylalcohol with benzyl benzoate

Citation
B. Nienhaus et al., Vapor-liquid equilibria at 453.25 K and excess enthalpies at 363.15 K and 413.15 K for mixtures of benzene, toluene, phenol, benzaldehyde, and benzylalcohol with benzyl benzoate, J CHEM EN D, 44(2), 1999, pp. 303-308
Citations number
13
Categorie Soggetti
Chemistry,"Chemical Engineering
Journal title
JOURNAL OF CHEMICAL AND ENGINEERING DATA
ISSN journal
00219568 → ACNP
Volume
44
Issue
2
Year of publication
1999
Pages
303 - 308
Database
ISI
SICI code
0021-9568(199903/04)44:2<303:VEA4KA>2.0.ZU;2-Y
Abstract
Isothermal P-x data at 453.25 K and excess enthalpies at 363.15 K and 413.1 5 K are presented for binary systems of benzyl benzoate together with benze ne, toluene, phenol, benzaldehyde, and benzyl alcohol. As pointed out previ ously (Nienhaus, B.; Limbeck, U.; Bolts, R.; de Haan, A. B.; Niemann, S. H. ; Gmehling, J. J. Chem. Eng. Data 1998, 43, 941-948), information about the real behavior of systems including these components is very important, esp ecially for the production of phenol by toluene oxidation. In addition, the se data will be used for the introduction of a new aromatic ester group (AC -COO-) into modified UNIFAC (Dortmund), which is part of the revision, exte nsion, and further development of this group contribution method. The vapor -liquid equilibrium (VLE) data of four systems were measured using a static apparatus. The corresponding experimental excess enthalpy (HE) data were d etermined with the help of an isothermal flow calorimeter. For the simultan eous description of VLE and HE data the NRTL model was used.