Thermodynamics of fuels with a biosynthetic component. II. Vapor-liquid equilibrium data for binary and ternary mixtures containing ethyl 1,1-dimethylethyl ether, 1-hexene, and cyclohexane at T=313.15 K
Villamanan, RM; Vega-Maza, D; Chamorro, CR; Villamanan, MA; Segovia, J
HERO ID
1249208
Reference Type
Journal Article
Year
2008
Language
English
| HERO ID | 1249208 |
|---|---|
| In Press | No |
| Year | 2008 |
| Title | Thermodynamics of fuels with a biosynthetic component. II. Vapor-liquid equilibrium data for binary and ternary mixtures containing ethyl 1,1-dimethylethyl ether, 1-hexene, and cyclohexane at T=313.15 K |
| Authors | Villamanan, RM; Vega-Maza, D; Chamorro, CR; Villamanan, MA; Segovia, J |
| Journal | Journal of Chemical and Engineering Data |
| Volume | 53 |
| Issue | 1 |
| Page Numbers | 247-251 |
| Abstract | Vapor-liquid equilibria, data containing ethyl 1, 1-dimethylethyl ether (ETBE) as an ether synthesized from ethanol of biological origin, are presented giving isothermal p-x-y data for the ternary system ethyl 1, 1 dimethylethyl ether (ETBE) + 1-hexene + cyclohexane and the two binary systems involved containing the ether at 313.15 K. A static technique consisting of an isothermal total pressure cell was used for the measurements. Data reduction by Barker's method provides correlations for G, using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL, and UNIQUAC models have also been alied to both binary and ternary systems. The mixtures measured exhibit a slight positive deviation from ideal behavior. |
| Doi | 10.1021/je7005488 |
| Wosid | WOS:000252292600045 |
| Is Certified Translation | No |
| Dupe Override | No |
| Comments | Source: Web of Science 000252292600045 |
| Is Public | Yes |
| Language Text | English |
| Keyword | TOTAL-PRESSURE DATA; SUBSTITUTION HYDROCARBONS; PLUS CYCLOHEXANE; N-HEPTANE; SYSTEMS; EXPRESSION; REDUCTION; ENERGY; HEXANE; GE |
| Is Qa | No |