Mixture of Dodecane + Ethylene oxide

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene oxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
302.52	0.2982	116.50
302.56	0.3994	140.80
302.56	0.5993	170.20
302.63	0.4994	155.60
302.63	0.6993	182.20
302.78	0.7994	190.00
332.30	0.2966	234.10
332.59	0.7989	452.50
332.66	0.4979	343.20
332.67	0.6986	421.60
332.78	0.5980	386.60
332.80	0.3978	294.80
333.72	0.1961	170.20
361.17	0.0964	143.80
362.62	0.2948	414.90
362.98	0.4961	648.00
363.09	0.5964	752.50
363.18	0.3960	539.30
363.59	0.6978	841.10
364.73	0.1938	293.20
369.77	0.2934	657.20
391.17	0.6975	1402.20
393.04	0.4947	1069.00
393.46	0.3946	871.60
395.18	0.1916	447.50

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene oxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
302.52	0.2982	116.50
302.56	0.3994	140.80
302.56	0.5993	170.20
302.63	0.4994	155.60
302.63	0.6993	182.20
302.78	0.7994	190.00
332.30	0.2966	234.10
332.59	0.7989	452.50
332.66	0.4979	343.20
332.67	0.6986	421.60
332.78	0.5980	386.60
332.80	0.3978	294.80
333.72	0.1961	170.20
361.17	0.0964	143.80
362.62	0.2948	414.90
362.98	0.4961	648.00
363.09	0.5964	752.50
363.18	0.3960	539.30
363.59	0.6978	841.10
364.73	0.1938	293.20
369.77	0.2934	657.20
391.17	0.6975	1402.20
393.04	0.4947	1069.00
393.46	0.3946	871.60
395.18	0.1916	447.50

Sources

• Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State