Mixture of Propane, 2-ethoxy-2-methyl- + Cyclohexane

Datasets

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

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0505	298.15	0.0505
0.0506	313.15	0.0476
0.1000	298.15	0.0987
0.1001	313.15	0.0917
0.1508	298.15	0.1434
0.1509	313.15	0.1363
0.2005	298.15	0.1812
0.2006	313.15	0.1744
0.2514	298.15	0.2170
0.2515	313.15	0.2091
0.3011	298.15	0.2469
0.3012	313.15	0.2350
0.3519	298.15	0.2730
0.3519	313.15	0.2610
0.4014	298.15	0.2940
0.4015	313.15	0.2826
0.4519	298.15	0.3099
0.4520	313.15	0.2947
0.5012	298.15	0.3185
0.5012	313.15	0.3049
0.5513	298.15	0.3233
0.5513	313.15	0.3078
0.6021	298.15	0.3198
0.6021	313.15	0.3060
0.6516	298.15	0.3091
0.6517	313.15	0.2962
0.7017	298.15	0.2931
0.7019	313.15	0.2798
0.7507	298.15	0.2691
0.7508	313.15	0.2577
0.8002	298.15	0.2359
0.8002	313.15	0.2240
0.8500	313.15	0.1838
0.8501	298.15	0.1943
0.9003	298.15	0.1420
0.9003	313.15	0.1342
0.9508	298.15	0.0761
0.9508	313.15	0.0730
1.0000	298.15	0.0000
1.0000	313.15	0.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0505	298.15	0.0505
0.0506	313.15	0.0476
0.1000	298.15	0.0987
0.1001	313.15	0.0917
0.1508	298.15	0.1434
0.1509	313.15	0.1363
0.2005	298.15	0.1812
0.2006	313.15	0.1744
0.2514	298.15	0.2170
0.2515	313.15	0.2091
0.3011	298.15	0.2469
0.3012	313.15	0.2350
0.3519	298.15	0.2730
0.3519	313.15	0.2610
0.4014	298.15	0.2940
0.4015	313.15	0.2826
0.4519	298.15	0.3099
0.4520	313.15	0.2947
0.5012	298.15	0.3185
0.5012	313.15	0.3049
0.5513	298.15	0.3233
0.5513	313.15	0.3078
0.6021	298.15	0.3198
0.6021	313.15	0.3060
0.6516	298.15	0.3091
0.6517	313.15	0.2962
0.7017	298.15	0.2931
0.7019	313.15	0.2798
0.7507	298.15	0.2691
0.7508	313.15	0.2577
0.8002	298.15	0.2359
0.8002	313.15	0.2240
0.8500	313.15	0.1838
0.8501	298.15	0.1943
0.9003	298.15	0.1420
0.9003	313.15	0.1342
0.9508	298.15	0.0761
0.9508	313.15	0.0730
1.0000	298.15	0.0000
1.0000	313.15	0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of Propane, 2-ethoxy-2-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	24.64
0.0596	25.45
0.0985	25.94
0.1499	26.52
0.2062	27.11
0.2499	27.52
0.3068	28.01
0.3496	28.36
0.4003	28.73
0.4011	28.74
0.4496	29.08
0.4498	29.07
0.5002	29.39
0.5050	29.44
0.5504	29.69
0.5518	29.72
0.5960	29.97
0.6006	29.98
0.6501	30.23
0.6987	30.48
0.7504	30.72
0.8013	30.93
0.8507	31.12
0.9006	31.31
0.9506	31.46
1.0000	31.62

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of Propane, 2-ethoxy-2-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	24.64
0.0596	25.45
0.0985	25.94
0.1499	26.52
0.2062	27.11
0.2499	27.52
0.3068	28.01
0.3496	28.36
0.4003	28.73
0.4011	28.74
0.4496	29.08
0.4498	29.07
0.5002	29.39
0.5050	29.44
0.5504	29.69
0.5518	29.72
0.5960	29.97
0.6006	29.98
0.6501	30.23
0.6987	30.48
0.7504	30.72
0.8013	30.93
0.8507	31.12
0.9006	31.31
0.9506	31.46
1.0000	31.62

Sources

• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• 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