Thermodynamic properties of organic oxygen compounds XXV. Vapour pressures and normal boiling temperatures of aliphatic alcohols

PVT Measurements for Pure Ethanol in the Near-Critical and Supercritical Regions

“…Vapor-pressure data for pure ethanol at high temperatures (above 373 K) were reported by various authors [10,11,13,[16][17][18][19][20][21][22][23][24][25][26][27][28][29][30][31]. Saturatedliquid and -vapor densities for ethanol (above 373 K) were also reported [10,11,13,21,27,[32][33][34][35][36][37][38][39][40].…”

Vapor pressure of heat transfer fluids of absorption refrigeration machines and heat pumps: Binary solutions of lithium nitrate with methanol

“…The measuring cell is equipped with an injection port. The temperature inside the cell was measured by a platinum resistance thermometer PT-100 (Type 42441-V100), connected to the signal conditioner Kelvimat Type 4303 (10), with an accuracy of T = ±0.01 K. The pressure was measured using a calibrated high accuracy sensor head (2) [Type 615A connected (7) to the signal conditioner Type 670A (8), MKS Baratron] attached to the top of the cell. The sensor head and the connecting line (5) from the cell to the sensor were thermostated (3) at T = 333.15 ± 0.01 K. The experimental uncertainties were DT = ±0.01 K for temperature and Dp = ±10 Pa for pressure.…”

Isothermal v.l.e. and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether,n -heptane and isopropanol at T= 313.15 K

“…Calculated from Antoine equation using constants reported by Riddick et al (29) ; b Calculated from Antoine equation using constants reported by Ambrose et al (30) ; c Calculated from Antoine equation using constants reported by Reid et al (31) ; d Calculated from Antoine equation using constants reported in TRC (32) ; e Reported by Montero (34) ; f Reported by Segovia (4) ; g Reported by Mara et al (35) ; h Reported by Ambrose et al (36) ; i Reported by Oracz (37) ; j Reported in TRC (32,33) ; k Calculated by Hayden et al (19) from Dymond et al (20) The non-ideality of the vapour phase is taken into account by the virial equation of state, truncated at the second term. The second virial coefficients have been calculated by the Hayden O'Connell method (22) using the coefficients given by Dymond et al (23) The ternary […”