Isothermal vapor-liquid equilibrium and excess enthalpy data for the binary systems methyl tert-butyl ether plus cyclohexane and ethyl tert-butyl ether plus cyclohexane, n-hexane, and n-heptane in a temperature range from 298.15 to 393.15 K

Citation
A. Del Rio et al., Isothermal vapor-liquid equilibrium and excess enthalpy data for the binary systems methyl tert-butyl ether plus cyclohexane and ethyl tert-butyl ether plus cyclohexane, n-hexane, and n-heptane in a temperature range from 298.15 to 393.15 K, J CHEM EN D, 46(5), 2001, pp. 1181-1187
Citations number
20
Categorie Soggetti
Chemistry,"Chemical Engineering
Journal title
JOURNAL OF CHEMICAL AND ENGINEERING DATA
ISSN journal
00219568 → ACNP
Volume
46
Issue
5
Year of publication
2001
Pages
1181 - 1187
Database
ISI
SICI code
0021-9568(200109/10)46:5<1181:IVEAEE>2.0.ZU;2-M
Abstract
Isothermal vapor-liquid equilibrium (VLE) and excess enthalpy (H-E) data ar e reported for binary systems containing branched ethers and hydrocarbons., The vapor-liquid equilibrium data for methyl tert-butyl ether (MTBE) + cyc lohexane at 308.15 K, for ethyl tert-butyl ether (ETBE) + cyclohexane, n-he xane + ethyl tert-butyl ether, and ethyl tert-butyl ether + n-heptane from 298.15 to 363.15 K were measured by means of a computer-controlled static a pparatus. An isothermal flow calorimeter was used to obtain excess enthalpy data for the systems containing ethyl tert-butyl ether at 313.15 and 393.1 5 K. The experimental VLE and H-E data were compared with the data of other authors and have been used simultaneously for the correlation of temperatu re-dependent UNIQUAC parameters.