Mixture of Diethyl carbonate + Cyclohexane

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_c - Critical pressure, kPa (2)
4. T_boil - Boiling temperature at pressure P, K (2)
5. T_c - Critical temperature, K (2)

Mole fraction of Cyclohexane (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0140	0.0770
0.0360	0.1840
0.0540	0.2630
0.0820	0.3580
0.1430	0.5000
0.1860	0.5810
0.2390	0.6550
0.3000	0.7090
0.3660	0.7490
0.4200	0.7790
0.4560	0.8020
0.5080	0.8200
0.5550	0.8390
0.6170	0.8570
0.6590	0.8750
0.7040	0.8870
0.7640	0.9020
0.8050	0.9160
0.8640	0.9360
0.9020	0.9510
0.9540	0.9730
0.9810	0.9890

Mole fraction of Cyclohexane (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0140	0.0770
0.0360	0.1840
0.0540	0.2630
0.0820	0.3580
0.1430	0.5000
0.1860	0.5810
0.2390	0.6550
0.3000	0.7090
0.3660	0.7490
0.4200	0.7790
0.4560	0.8020
0.5080	0.8200
0.5550	0.8390
0.6170	0.8570
0.6590	0.8750
0.7040	0.8870
0.7640	0.9020
0.8050	0.9160
0.8640	0.9360
0.9020	0.9510
0.9540	0.9730
0.9810	0.9890

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0501	0.0009
293.15	0.0992	0.0008
293.15	0.1969	0.0008
293.15	0.2923	0.0007
293.15	0.4023	0.0007
293.15	0.5020	0.0007
293.15	0.5984	0.0007
293.15	0.6977	0.0007
293.15	0.8080	0.0007
293.15	0.9037	0.0008
293.15	0.9511	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0009
298.15	0.0531	0.0008
298.15	0.0940	0.0008
298.15	0.1931	0.0007
298.15	0.2865	0.0007
298.15	0.3821	0.0007
298.15	0.4802	0.0007
298.15	0.6454	0.0007
298.15	0.6801	0.0007
298.15	0.7828	0.0007
298.15	0.8852	0.0007
298.15	0.9177	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0008
303.15	0.0497	0.0008
303.15	0.1018	0.0007
303.15	0.1958	0.0007
303.15	0.2930	0.0006
303.15	0.3922	0.0006
303.15	0.4767	0.0006
303.15	0.5943	0.0006
303.15	0.6778	0.0006
303.15	0.7897	0.0007
303.15	0.8649	0.0007
303.15	0.9400	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0007
313.15	0.0511	0.0007
313.15	0.0983	0.0006
313.15	0.2003	0.0006
313.15	0.3002	0.0006
313.15	0.3963	0.0006
313.15	0.4953	0.0006
313.15	0.5914	0.0006
313.15	0.7001	0.0006
313.15	0.8098	0.0006
313.15	0.9014	0.0006
313.15	0.9494	0.0006
313.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0501	0.0009
293.15	0.0992	0.0008
293.15	0.1969	0.0008
293.15	0.2923	0.0007
293.15	0.4023	0.0007
293.15	0.5020	0.0007
293.15	0.5984	0.0007
293.15	0.6977	0.0007
293.15	0.8080	0.0007
293.15	0.9037	0.0008
293.15	0.9511	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0009
298.15	0.0531	0.0008
298.15	0.0940	0.0008
298.15	0.1931	0.0007
298.15	0.2865	0.0007
298.15	0.3821	0.0007
298.15	0.4802	0.0007
298.15	0.6454	0.0007
298.15	0.6801	0.0007
298.15	0.7828	0.0007
298.15	0.8852	0.0007
298.15	0.9177	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0008
303.15	0.0497	0.0008
303.15	0.1018	0.0007
303.15	0.1958	0.0007
303.15	0.2930	0.0006
303.15	0.3922	0.0006
303.15	0.4767	0.0006
303.15	0.5943	0.0006
303.15	0.6778	0.0006
303.15	0.7897	0.0007
303.15	0.8649	0.0007
303.15	0.9400	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0007
313.15	0.0511	0.0007
313.15	0.0983	0.0006
313.15	0.2003	0.0006
313.15	0.3002	0.0006
313.15	0.3963	0.0006
313.15	0.4953	0.0006
313.15	0.5914	0.0006
313.15	0.7001	0.0006
313.15	0.8098	0.0006
313.15	0.9014	0.0006
313.15	0.9494	0.0006
313.15	1.0000	0.0006

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0734	3968.00
0.1512	3891.00
0.2339	3832.00
0.3220	3782.00
0.4160	3736.00
0.5166	3678.00
0.6244	3609.00
0.7402	3513.00
0.8651	3414.00

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0734	3968.00
0.1512	3891.00
0.2339	3832.00
0.3220	3782.00
0.4160	3736.00
0.5166	3678.00
0.6244	3609.00
0.7402	3513.00
0.8651	3414.00

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0140	396.14
0.0360	392.79
0.0540	390.27
0.0820	386.59
0.1430	380.74
0.1860	376.41
0.2390	372.83
0.3000	369.80
0.3660	366.91
0.4200	364.92
0.4560	363.59
0.5080	362.22
0.5550	360.85
0.6170	359.61
0.6590	358.68
0.7040	357.74
0.7640	356.74
0.8050	356.16
0.8640	355.27
0.9020	354.67
0.9540	353.94
0.9810	353.64

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0140	396.14
0.0360	392.79
0.0540	390.27
0.0820	386.59
0.1430	380.74
0.1860	376.41
0.2390	372.83
0.3000	369.80
0.3660	366.91
0.4200	364.92
0.4560	363.59
0.5080	362.22
0.5550	360.85
0.6170	359.61
0.6590	358.68
0.7040	357.74
0.7640	356.74
0.8050	356.16
0.8640	355.27
0.9020	354.67
0.9540	353.94
0.9810	353.64

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0734	552.70
0.1512	552.50
0.2339	553.30
0.3220	553.60
0.4160	556.70
0.5166	559.70
0.6244	564.20
0.7402	568.70
0.8651	574.90

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0734	552.70
0.1512	552.50
0.2339	553.30
0.3220	553.60
0.4160	556.70
0.5166	559.70
0.6244	564.20
0.7402	568.70
0.8651	574.90

Sources

• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer