Mixture of Ethanol + Cyclohexane

Datasets

1. Mole fraction (12)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. η - Viscosity, Pa*s (2)
4. Excess molar enthalpy (molar enthalpy (2)
5. P_vap - Vapor or sublimation pressure, kPa (2)
6. ρ_l - Mass density, kg/m3 (4)
7. c_sound,fluid - Speed of Sound, m/s (2)
8. T_boil - Boiling temperature at pressure P, K (6)
9. Binary diffusion coefficient, m2/s (2)
10. Vapor Liquid Equilibrium at Constant Temperature (3)

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0200	0.2220
0.2020	0.4020
0.4420	0.4180
0.5600	0.4510
0.7220	0.4890
0.7880	0.4860
0.8290	0.5500
0.8820	0.6250
0.9060	0.6580
0.9330	0.7030
0.9490	0.7500
0.9720	0.8180
0.9780	0.8770
0.9900	0.9470

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
101.30	0.4540

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
337.95	0.4540

Mole fraction of Cyclohexane (2) [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0000	40.00	0.0000
0.0130	40.00	0.1100
0.1170	40.00	0.4650
0.1740	40.00	0.5320
0.2410	40.00	0.5770
0.5080	40.00	0.6240
0.5600	40.00	0.6250
0.7050	40.00	0.6370
0.7430	40.00	0.6420
0.7880	40.00	0.6500
0.8960	40.00	0.6630
0.9460	40.00	0.6940
0.9720	40.00	0.7350
0.9800	40.00	0.7690
1.0000	40.00	1.0000
0.0000	69.81	0.0000
0.0150	69.81	0.0990
0.0640	69.81	0.3090
0.1280	69.81	0.4120
0.1860	69.81	0.4820
0.2510	69.81	0.5230
0.4240	69.81	0.5730
0.5040	69.81	0.5820
0.5660	69.81	0.5840
0.7150	69.81	0.6000
0.7920	69.81	0.6060
0.8600	69.81	0.6190
0.9110	69.81	0.6380
0.9390	69.81	0.6650
0.9660	69.81	0.7290
0.9890	69.81	0.8790
1.0000	69.81	1.0000
0.0000	97.72	0.0000
0.0640	97.72	0.2740
0.1260	97.72	0.3870
0.1870	97.72	0.4530
0.3630	97.72	0.5270
0.4300	97.72	0.5460
0.5690	97.72	0.5600
0.7190	97.72	0.5790
0.7570	97.72	0.5800
0.7740	97.72	0.5810
0.8510	97.72	0.5980
0.9030	97.72	0.6190
0.9590	97.72	0.7390
0.9910	97.72	0.8970
1.0000	97.72	1.0000
0.0000	150.00	0.0000
0.0680	150.00	0.2420
0.1310	150.00	0.3560
0.1950	150.00	0.4130
0.2440	150.00	0.4550
0.3640	150.00	0.4920
0.5160	150.00	0.5220
0.5720	150.00	0.5290
0.7190	150.00	0.5540
0.7990	150.00	0.5930
0.9170	150.00	0.6750
1.0000	150.00	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.9973	0.8973
0.9890	0.8431
0.9742	0.7960
0.9499	0.7230
0.9119	0.6520
0.8775	0.5942
0.8280	0.5361
0.7849	0.5084
0.6917	0.4763
0.6425	0.4742
0.5693	0.4668
0.5401	0.4564
0.4345	0.4482
0.3227	0.4457
0.2734	0.4530
0.1393	0.4680
0.0648	0.4281
0.0526	0.4052
0.0352	0.3595
0.0303	0.3160
0.0245	0.2870
0.0192	0.2332
0.0157	0.2066
0.0144	0.1341
0.0102	0.0688

Mole fraction of Cyclohexane (2) [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0210	0.1600
0.0430	0.2500
0.2000	0.5090
0.4400	0.5580
0.5360	0.5700
0.5910	0.5920
0.5930	0.5950
0.6690	0.6030
0.8120	0.6210
0.8820	0.6330
0.9060	0.6490
0.9570	0.7180
0.9820	0.8240

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0200	0.2220
0.2020	0.4020
0.4420	0.4180
0.5600	0.4510
0.7220	0.4890
0.7880	0.4860
0.8290	0.5500
0.8820	0.6250
0.9060	0.6580
0.9330	0.7030
0.9490	0.7500
0.9720	0.8180
0.9780	0.8770
0.9900	0.9470

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
101.30	0.4540

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
337.95	0.4540

Mole fraction of Cyclohexane (2) [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0000	40.00	0.0000
0.0130	40.00	0.1100
0.1170	40.00	0.4650
0.1740	40.00	0.5320
0.2410	40.00	0.5770
0.5080	40.00	0.6240
0.5600	40.00	0.6250
0.7050	40.00	0.6370
0.7430	40.00	0.6420
0.7880	40.00	0.6500
0.8960	40.00	0.6630
0.9460	40.00	0.6940
0.9720	40.00	0.7350
0.9800	40.00	0.7690
1.0000	40.00	1.0000
0.0000	69.81	0.0000
0.0150	69.81	0.0990
0.0640	69.81	0.3090
0.1280	69.81	0.4120
0.1860	69.81	0.4820
0.2510	69.81	0.5230
0.4240	69.81	0.5730
0.5040	69.81	0.5820
0.5660	69.81	0.5840
0.7150	69.81	0.6000
0.7920	69.81	0.6060
0.8600	69.81	0.6190
0.9110	69.81	0.6380
0.9390	69.81	0.6650
0.9660	69.81	0.7290
0.9890	69.81	0.8790
1.0000	69.81	1.0000
0.0000	97.72	0.0000
0.0640	97.72	0.2740
0.1260	97.72	0.3870
0.1870	97.72	0.4530
0.3630	97.72	0.5270
0.4300	97.72	0.5460
0.5690	97.72	0.5600
0.7190	97.72	0.5790
0.7570	97.72	0.5800
0.7740	97.72	0.5810
0.8510	97.72	0.5980
0.9030	97.72	0.6190
0.9590	97.72	0.7390
0.9910	97.72	0.8970
1.0000	97.72	1.0000
0.0000	150.00	0.0000
0.0680	150.00	0.2420
0.1310	150.00	0.3560
0.1950	150.00	0.4130
0.2440	150.00	0.4550
0.3640	150.00	0.4920
0.5160	150.00	0.5220
0.5720	150.00	0.5290
0.7190	150.00	0.5540
0.7990	150.00	0.5930
0.9170	150.00	0.6750
1.0000	150.00	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.9973	0.8973
0.9890	0.8431
0.9742	0.7960
0.9499	0.7230
0.9119	0.6520
0.8775	0.5942
0.8280	0.5361
0.7849	0.5084
0.6917	0.4763
0.6425	0.4742
0.5693	0.4668
0.5401	0.4564
0.4345	0.4482
0.3227	0.4457
0.2734	0.4530
0.1393	0.4680
0.0648	0.4281
0.0526	0.4052
0.0352	0.3595
0.0303	0.3160
0.0245	0.2870
0.0192	0.2332
0.0157	0.2066
0.0144	0.1341
0.0102	0.0688

Mole fraction of Cyclohexane (2) [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mole fraction of Cyclohexane (2) - Gas
0.0210	0.1600
0.0430	0.2500
0.2000	0.5090
0.4400	0.5580
0.5360	0.5700
0.5910	0.5920
0.5930	0.5950
0.6690	0.6030
0.8120	0.6210
0.8820	0.6330
0.9060	0.6490
0.9570	0.7180
0.9820	0.8240

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
100.00	0.0000	119.20
100.00	0.1000	127.80
100.00	0.1999	134.20
100.00	0.2999	140.20
100.00	0.4000	146.90
100.00	0.5002	152.70
100.00	0.6000	158.20
100.00	0.7002	163.30
100.00	0.8000	167.60
100.00	0.8999	169.90
100.00	1.0000	162.70
5000.00	0.0000	118.00
5000.00	0.1000	126.50
5000.00	0.1999	132.90
5000.00	0.2999	138.80
5000.00	0.4000	145.20
5000.00	0.5002	151.00
5000.00	0.6000	155.90
5000.00	0.7002	161.00
5000.00	0.8000	165.20
5000.00	0.8999	167.30
5000.00	1.0000	160.70
10000.00	0.0000	116.80
10000.00	0.1000	125.00
10000.00	0.1999	131.00
10000.00	0.2999	137.10
10000.00	0.4000	143.10
10000.00	0.5002	149.00
10000.00	0.6000	154.00
10000.00	0.7002	159.00
10000.00	0.8000	163.10
10000.00	0.8999	165.50
10000.00	1.0000	158.80
15000.00	0.0000	115.50
15000.00	0.1000	123.70
15000.00	0.1999	130.20
15000.00	0.2999	135.70
15000.00	0.4000	141.30
15000.00	0.5002	147.00
15000.00	0.6000	152.90
15000.00	0.7002	157.60
15000.00	0.8000	161.30
15000.00	0.8999	163.30
15000.00	1.0000	157.30
20000.00	0.0000	114.90
20000.00	0.1000	122.80
20000.00	0.1999	129.50
20000.00	0.2999	134.90
20000.00	0.4000	140.70
20000.00	0.5002	146.60
20000.00	0.6000	149.00
20000.00	0.7002	156.30
20000.00	0.8000	160.50
20000.00	0.8999	162.50
20000.00	1.0000	155.90

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
100.00	0.0000	119.20
100.00	0.1000	127.80
100.00	0.1999	134.20
100.00	0.2999	140.20
100.00	0.4000	146.90
100.00	0.5002	152.70
100.00	0.6000	158.20
100.00	0.7002	163.30
100.00	0.8000	167.60
100.00	0.8999	169.90
100.00	1.0000	162.70
5000.00	0.0000	118.00
5000.00	0.1000	126.50
5000.00	0.1999	132.90
5000.00	0.2999	138.80
5000.00	0.4000	145.20
5000.00	0.5002	151.00
5000.00	0.6000	155.90
5000.00	0.7002	161.00
5000.00	0.8000	165.20
5000.00	0.8999	167.30
5000.00	1.0000	160.70
10000.00	0.0000	116.80
10000.00	0.1000	125.00
10000.00	0.1999	131.00
10000.00	0.2999	137.10
10000.00	0.4000	143.10
10000.00	0.5002	149.00
10000.00	0.6000	154.00
10000.00	0.7002	159.00
10000.00	0.8000	163.10
10000.00	0.8999	165.50
10000.00	1.0000	158.80
15000.00	0.0000	115.50
15000.00	0.1000	123.70
15000.00	0.1999	130.20
15000.00	0.2999	135.70
15000.00	0.4000	141.30
15000.00	0.5002	147.00
15000.00	0.6000	152.90
15000.00	0.7002	157.60
15000.00	0.8000	161.30
15000.00	0.8999	163.30
15000.00	1.0000	157.30
20000.00	0.0000	114.90
20000.00	0.1000	122.80
20000.00	0.1999	129.50
20000.00	0.2999	134.90
20000.00	0.4000	140.70
20000.00	0.5002	146.60
20000.00	0.6000	149.00
20000.00	0.7002	156.30
20000.00	0.8000	160.50
20000.00	0.8999	162.50
20000.00	1.0000	155.90

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0012
293.15	0.0473	0.0011
293.15	0.0960	0.0011
293.15	0.2043	0.0011
293.15	0.3028	0.0010
293.15	0.3979	0.0010
293.15	0.5027	0.0010
293.15	0.5939	0.0009
293.15	0.7051	0.0009
293.15	0.8055	0.0009
293.15	0.9041	0.0009
293.15	0.9534	0.0009
293.15	1.0000	0.0010
298.15	0.0000	0.0011
298.15	0.0473	0.0010
298.15	0.0960	0.0010
298.15	0.2043	0.0010
298.15	0.3028	0.0009
298.15	0.3979	0.0009
298.15	0.5027	0.0009
298.15	0.5939	0.0009
298.15	0.7051	0.0008
298.15	0.8055	0.0008
298.15	0.9041	0.0008
298.15	0.9534	0.0009
298.15	1.0000	0.0009
303.15	0.0000	0.0010
303.15	0.0473	0.0010
303.15	0.0960	0.0009
303.15	0.2043	0.0009
303.15	0.3028	0.0008
303.15	0.3979	0.0008
303.15	0.5027	0.0008
303.15	0.5939	0.0008
303.15	0.7051	0.0008
303.15	0.8055	0.0008
303.15	0.9041	0.0008
303.15	0.9534	0.0008
303.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0012
293.15	0.0473	0.0011
293.15	0.0960	0.0011
293.15	0.2043	0.0011
293.15	0.3028	0.0010
293.15	0.3979	0.0010
293.15	0.5027	0.0010
293.15	0.5939	0.0009
293.15	0.7051	0.0009
293.15	0.8055	0.0009
293.15	0.9041	0.0009
293.15	0.9534	0.0009
293.15	1.0000	0.0010
298.15	0.0000	0.0011
298.15	0.0473	0.0010
298.15	0.0960	0.0010
298.15	0.2043	0.0010
298.15	0.3028	0.0009
298.15	0.3979	0.0009
298.15	0.5027	0.0009
298.15	0.5939	0.0009
298.15	0.7051	0.0008
298.15	0.8055	0.0008
298.15	0.9041	0.0008
298.15	0.9534	0.0009
298.15	1.0000	0.0009
303.15	0.0000	0.0010
303.15	0.0473	0.0010
303.15	0.0960	0.0009
303.15	0.2043	0.0009
303.15	0.3028	0.0008
303.15	0.3979	0.0008
303.15	0.5027	0.0008
303.15	0.5939	0.0008
303.15	0.7051	0.0008
303.15	0.8055	0.0008
303.15	0.9041	0.0008
303.15	0.9534	0.0008
303.15	1.0000	0.0008

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

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0320	0.4450
0.0540	0.5540
0.1020	0.7070
0.1510	0.8050
0.2020	0.8680
0.2510	0.9070
0.3000	0.9350
0.3510	0.9470
0.4010	0.9460
0.4520	0.9330
0.5000	0.9100
0.5510	0.8740
0.6010	0.8290
0.6500	0.7740
0.7070	0.6900
0.7500	0.6280
0.8020	0.5310
0.8510	0.4240
0.9010	0.3020
0.9510	0.1590

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

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0320	0.4450
0.0540	0.5540
0.1020	0.7070
0.1510	0.8050
0.2020	0.8680
0.2510	0.9070
0.3000	0.9350
0.3510	0.9470
0.4010	0.9460
0.4520	0.9330
0.5000	0.9100
0.5510	0.8740
0.6010	0.8290
0.6500	0.7740
0.7070	0.6900
0.7500	0.6280
0.8020	0.5310
0.8510	0.4240
0.9010	0.3020
0.9510	0.1590

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0210	35.97
0.0430	39.65
0.2000	53.65
0.4400	56.55
0.5360	57.44
0.5910	57.67
0.5930	57.68
0.6690	57.73
0.8120	57.20
0.8820	56.30
0.9060	54.79
0.9570	51.10
0.9820	45.88

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0210	35.97
0.0430	39.65
0.2000	53.65
0.4400	56.55
0.5360	57.44
0.5910	57.67
0.5930	57.68
0.6690	57.73
0.8120	57.20
0.8820	56.30
0.9060	54.79
0.9570	51.10
0.9820	45.88

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	789.75
293.15	0.0473	787.0
293.15	0.0960	784.97
293.15	0.2043	781.33
293.15	0.3028	779.4
293.15	0.3979	778.2
293.15	0.5027	777.4
293.15	0.5939	776.98
293.15	0.7051	776.79
293.15	0.8055	776.89
293.15	0.9041	777.3
293.15	0.9534	777.74
293.15	1.0000	778.62
298.15	0.0000	785.46
298.15	0.0473	782.65
298.15	0.0960	780.6
298.15	0.2043	776.87
298.15	0.3028	774.86
298.15	0.3979	773.6
298.15	0.5027	772.73
298.15	0.5939	772.26
298.15	0.7051	772.03
298.15	0.8055	772.11
298.15	0.9041	772.5
298.15	0.9534	772.98
298.15	1.0000	773.92
303.15	0.0000	781.15
303.15	0.0473	778.29
303.15	0.0960	776.2
303.15	0.2043	772.37
303.15	0.3028	770.28
303.15	0.3979	768.95
303.15	0.5027	768.0
303.15	0.5939	767.49
303.15	0.7051	767.22
303.15	0.8055	767.28
303.15	0.9041	767.8
303.15	0.9534	768.18
303.15	1.0000	769.19

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	0.2999	788.5
283.15	1000.00	0.2999	789.2
283.15	2000.00	0.2999	790.0
283.15	5000.00	0.2999	792.5
283.15	10000.00	0.2999	796.4
283.15	15000.00	0.2999	800.0
283.15	20000.00	0.2999	803.5
293.15	100.00	0.2999	779.6
293.15	1000.00	0.2999	780.4
293.15	2000.00	0.2999	781.3
293.15	5000.00	0.2999	783.9
293.15	10000.00	0.2999	788.0
293.15	15000.00	0.2999	791.9
293.15	20000.00	0.2999	795.6
313.15	100.00	0.2999	761.2
313.15	1000.00	0.2999	762.0
313.15	2000.00	0.2999	763.0
313.15	5000.00	0.2999	766.0
313.15	10000.00	0.2999	770.5
313.15	15000.00	0.2999	774.9
313.15	20000.00	0.2999	779.1
333.15	100.00	0.2999	742.0
333.15	1000.00	0.2999	743.0
333.15	2000.00	0.2999	744.1
333.15	5000.00	0.2999	747.5
333.15	10000.00	0.2999	752.8
333.15	15000.00	0.2999	757.6
333.15	20000.00	0.2999	762.3
283.15	100.00	0.5002	786.7
283.15	1000.00	0.5002	787.5
283.15	2000.00	0.5002	788.3
283.15	5000.00	0.5002	790.7
283.15	10000.00	0.5002	794.5
283.15	15000.00	0.5002	798.1
283.15	20000.00	0.5002	801.6
293.15	100.00	0.5002	777.6
293.15	1000.00	0.5002	778.4
293.15	2000.00	0.5002	779.2
293.15	5000.00	0.5002	781.8
293.15	10000.00	0.5002	785.8
293.15	15000.00	0.5002	789.7
293.15	20000.00	0.5002	793.4
313.15	100.00	0.5002	758.5
313.15	1000.00	0.5002	759.4
313.15	2000.00	0.5002	760.4
313.15	5000.00	0.5002	763.3
313.15	10000.00	0.5002	767.9
313.15	15000.00	0.5002	772.2
313.15	20000.00	0.5002	776.4
333.15	100.00	0.5002	738.7
333.15	1000.00	0.5002	739.7
333.15	2000.00	0.5002	740.9
333.15	5000.00	0.5002	744.3
333.15	10000.00	0.5002	749.6
333.15	15000.00	0.5002	754.5
333.15	20000.00	0.5002	759.2
283.15	100.00	0.7002	786.3
283.15	1000.00	0.7002	787.1
283.15	2000.00	0.7002	787.8
283.15	5000.00	0.7002	790.2
283.15	10000.00	0.7002	794.0
283.15	15000.00	0.7002	797.5
283.15	20000.00	0.7002	801.0
293.15	100.00	0.7002	777.0
293.15	1000.00	0.7002	777.8
293.15	2000.00	0.7002	778.6
293.15	5000.00	0.7002	781.1
293.15	10000.00	0.7002	785.1
293.15	15000.00	0.7002	788.9
293.15	20000.00	0.7002	792.6
313.15	100.00	0.7002	757.6
313.15	1000.00	0.7002	758.4
313.15	2000.00	0.7002	759.4
313.15	5000.00	0.7002	762.3
313.15	10000.00	0.7002	766.9
313.15	15000.00	0.7002	771.2
313.15	20000.00	0.7002	775.3
333.15	100.00	0.7002	737.5
333.15	1000.00	0.7002	738.5
333.15	2000.00	0.7002	739.7
333.15	5000.00	0.7002	743.1
333.15	10000.00	0.7002	748.3
333.15	15000.00	0.7002	753.2
333.15	20000.00	0.7002	757.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	789.75
293.15	0.0473	787.0
293.15	0.0960	784.97
293.15	0.2043	781.33
293.15	0.3028	779.4
293.15	0.3979	778.2
293.15	0.5027	777.4
293.15	0.5939	776.98
293.15	0.7051	776.79
293.15	0.8055	776.89
293.15	0.9041	777.3
293.15	0.9534	777.74
293.15	1.0000	778.62
298.15	0.0000	785.46
298.15	0.0473	782.65
298.15	0.0960	780.6
298.15	0.2043	776.87
298.15	0.3028	774.86
298.15	0.3979	773.6
298.15	0.5027	772.73
298.15	0.5939	772.26
298.15	0.7051	772.03
298.15	0.8055	772.11
298.15	0.9041	772.5
298.15	0.9534	772.98
298.15	1.0000	773.92
303.15	0.0000	781.15
303.15	0.0473	778.29
303.15	0.0960	776.2
303.15	0.2043	772.37
303.15	0.3028	770.28
303.15	0.3979	768.95
303.15	0.5027	768.0
303.15	0.5939	767.49
303.15	0.7051	767.22
303.15	0.8055	767.28
303.15	0.9041	767.8
303.15	0.9534	768.18
303.15	1.0000	769.19

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	0.2999	788.5
283.15	1000.00	0.2999	789.2
283.15	2000.00	0.2999	790.0
283.15	5000.00	0.2999	792.5
283.15	10000.00	0.2999	796.4
283.15	15000.00	0.2999	800.0
283.15	20000.00	0.2999	803.5
293.15	100.00	0.2999	779.6
293.15	1000.00	0.2999	780.4
293.15	2000.00	0.2999	781.3
293.15	5000.00	0.2999	783.9
293.15	10000.00	0.2999	788.0
293.15	15000.00	0.2999	791.9
293.15	20000.00	0.2999	795.6
313.15	100.00	0.2999	761.2
313.15	1000.00	0.2999	762.0
313.15	2000.00	0.2999	763.0
313.15	5000.00	0.2999	766.0
313.15	10000.00	0.2999	770.5
313.15	15000.00	0.2999	774.9
313.15	20000.00	0.2999	779.1
333.15	100.00	0.2999	742.0
333.15	1000.00	0.2999	743.0
333.15	2000.00	0.2999	744.1
333.15	5000.00	0.2999	747.5
333.15	10000.00	0.2999	752.8
333.15	15000.00	0.2999	757.6
333.15	20000.00	0.2999	762.3
283.15	100.00	0.5002	786.7
283.15	1000.00	0.5002	787.5
283.15	2000.00	0.5002	788.3
283.15	5000.00	0.5002	790.7
283.15	10000.00	0.5002	794.5
283.15	15000.00	0.5002	798.1
283.15	20000.00	0.5002	801.6
293.15	100.00	0.5002	777.6
293.15	1000.00	0.5002	778.4
293.15	2000.00	0.5002	779.2
293.15	5000.00	0.5002	781.8
293.15	10000.00	0.5002	785.8
293.15	15000.00	0.5002	789.7
293.15	20000.00	0.5002	793.4
313.15	100.00	0.5002	758.5
313.15	1000.00	0.5002	759.4
313.15	2000.00	0.5002	760.4
313.15	5000.00	0.5002	763.3
313.15	10000.00	0.5002	767.9
313.15	15000.00	0.5002	772.2
313.15	20000.00	0.5002	776.4
333.15	100.00	0.5002	738.7
333.15	1000.00	0.5002	739.7
333.15	2000.00	0.5002	740.9
333.15	5000.00	0.5002	744.3
333.15	10000.00	0.5002	749.6
333.15	15000.00	0.5002	754.5
333.15	20000.00	0.5002	759.2
283.15	100.00	0.7002	786.3
283.15	1000.00	0.7002	787.1
283.15	2000.00	0.7002	787.8
283.15	5000.00	0.7002	790.2
283.15	10000.00	0.7002	794.0
283.15	15000.00	0.7002	797.5
283.15	20000.00	0.7002	801.0
293.15	100.00	0.7002	777.0
293.15	1000.00	0.7002	777.8
293.15	2000.00	0.7002	778.6
293.15	5000.00	0.7002	781.1
293.15	10000.00	0.7002	785.1
293.15	15000.00	0.7002	788.9
293.15	20000.00	0.7002	792.6
313.15	100.00	0.7002	757.6
313.15	1000.00	0.7002	758.4
313.15	2000.00	0.7002	759.4
313.15	5000.00	0.7002	762.3
313.15	10000.00	0.7002	766.9
313.15	15000.00	0.7002	771.2
313.15	20000.00	0.7002	775.3
333.15	100.00	0.7002	737.5
333.15	1000.00	0.7002	738.5
333.15	2000.00	0.7002	739.7
333.15	5000.00	0.7002	743.1
333.15	10000.00	0.7002	748.3
333.15	15000.00	0.7002	753.2
333.15	20000.00	0.7002	757.9

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1162.0
293.15	0.0473	1162.0
293.15	0.0960	1165.0
293.15	0.2043	1174.0
293.15	0.3028	1184.0
293.15	0.3979	1195.0
293.15	0.5027	1208.0
293.15	0.5939	1219.0
293.15	0.7051	1232.0
293.15	0.8055	1245.0
293.15	0.9041	1258.0
293.15	0.9534	1267.0
293.15	1.0000	1279.0
298.15	0.0000	1145.0
298.15	0.0473	1144.0
298.15	0.0960	1147.0
298.15	0.2043	1155.0
298.15	0.3028	1164.0
298.15	0.3979	1174.0
298.15	0.5027	1186.0
298.15	0.5939	1196.0
298.15	0.7051	1209.0
298.15	0.8055	1221.0
298.15	0.9041	1235.0
298.15	0.9534	1242.0
298.15	1.0000	1254.0
303.15	0.0000	1128.0
303.15	0.0473	1127.0
303.15	0.0960	1129.0
303.15	0.2043	1135.0
303.15	0.3028	1144.0
303.15	0.3979	1153.0
303.15	0.5027	1164.0
303.15	0.5939	1174.0
303.15	0.7051	1186.0
303.15	0.8055	1197.0
303.15	0.9041	1211.0
303.15	0.9534	1218.0
303.15	1.0000	1230.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1162.0
293.15	0.0473	1162.0
293.15	0.0960	1165.0
293.15	0.2043	1174.0
293.15	0.3028	1184.0
293.15	0.3979	1195.0
293.15	0.5027	1208.0
293.15	0.5939	1219.0
293.15	0.7051	1232.0
293.15	0.8055	1245.0
293.15	0.9041	1258.0
293.15	0.9534	1267.0
293.15	1.0000	1279.0
298.15	0.0000	1145.0
298.15	0.0473	1144.0
298.15	0.0960	1147.0
298.15	0.2043	1155.0
298.15	0.3028	1164.0
298.15	0.3979	1174.0
298.15	0.5027	1186.0
298.15	0.5939	1196.0
298.15	0.7051	1209.0
298.15	0.8055	1221.0
298.15	0.9041	1235.0
298.15	0.9534	1242.0
298.15	1.0000	1254.0
303.15	0.0000	1128.0
303.15	0.0473	1127.0
303.15	0.0960	1129.0
303.15	0.2043	1135.0
303.15	0.3028	1144.0
303.15	0.3979	1153.0
303.15	0.5027	1164.0
303.15	0.5939	1174.0
303.15	0.7051	1186.0
303.15	0.8055	1197.0
303.15	0.9041	1211.0
303.15	0.9534	1218.0
303.15	1.0000	1230.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0200	347.42
0.2020	338.37
0.4420	338.08
0.5600	338.25
0.7220	338.55
0.7880	339.06
0.8290	340.08
0.8820	341.46
0.9060	342.31
0.9330	344.26
0.9490	345.48
0.9720	348.47
0.9780	348.56
0.9900	350.50

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	40.00	329.71
0.0130	40.00	327.21
0.1170	40.00	318.50
0.1740	40.00	316.88
0.2410	40.00	315.97
0.5080	40.00	314.80
0.5600	40.00	314.68
0.7050	40.00	314.70
0.7430	40.00	314.82
0.7880	40.00	314.81
0.8960	40.00	315.51
0.9460	40.00	316.30
0.9720	40.00	317.58
0.9800	40.00	318.71
1.0000	40.00	325.81
0.0000	69.81	342.30
0.0150	69.81	340.04
0.0640	69.81	335.05
0.1280	69.81	331.87
0.1860	69.81	330.31
0.2510	69.81	329.39
0.4240	69.81	328.66
0.5040	69.81	328.53
0.5660	69.81	328.52
0.7150	69.81	328.60
0.7920	69.81	328.67
0.8600	69.81	329.04
0.9110	69.81	329.70
0.9390	69.81	330.67
0.9660	69.81	332.49
0.9890	69.81	337.70
1.0000	69.81	341.99
0.0000	97.72	350.50
0.0640	97.72	343.56
0.1260	97.72	340.46
0.1870	97.72	338.99
0.3630	97.72	337.57
0.4300	97.72	337.37
0.5690	97.72	337.28
0.7190	97.72	337.42
0.7570	97.72	337.43
0.7740	97.72	337.46
0.8510	97.72	338.06
0.9030	97.72	338.78
0.9590	97.72	342.82
0.9910	97.72	348.82
1.0000	97.72	352.60
0.0000	150.00	361.71
0.0680	150.00	355.17
0.1310	150.00	352.24
0.1950	150.00	350.75
0.2440	150.00	350.02
0.3640	150.00	349.44
0.5160	150.00	349.21
0.5720	150.00	349.23
0.7190	150.00	349.51
0.7990	150.00	350.54
0.9170	150.00	354.19
1.0000	150.00	367.66

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9973	348.85
0.9890	347.55
0.9742	346.55
0.9499	344.75
0.9119	342.75
0.8775	341.45
0.8280	340.05
0.7849	339.35
0.6917	338.55
0.6425	338.35
0.5693	337.95
0.5401	337.85
0.4345	337.65
0.3227	337.75
0.2734	337.85
0.1393	338.75
0.0648	340.55
0.0526	342.15
0.0352	345.75
0.0303	347.65
0.0245	348.65
0.0192	350.15
0.0157	351.35
0.0144	352.75
0.0102	353.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0200	347.42
0.2020	338.37
0.4420	338.08
0.5600	338.25
0.7220	338.55
0.7880	339.06
0.8290	340.08
0.8820	341.46
0.9060	342.31
0.9330	344.26
0.9490	345.48
0.9720	348.47
0.9780	348.56
0.9900	350.50

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	40.00	329.71
0.0130	40.00	327.21
0.1170	40.00	318.50
0.1740	40.00	316.88
0.2410	40.00	315.97
0.5080	40.00	314.80
0.5600	40.00	314.68
0.7050	40.00	314.70
0.7430	40.00	314.82
0.7880	40.00	314.81
0.8960	40.00	315.51
0.9460	40.00	316.30
0.9720	40.00	317.58
0.9800	40.00	318.71
1.0000	40.00	325.81
0.0000	69.81	342.30
0.0150	69.81	340.04
0.0640	69.81	335.05
0.1280	69.81	331.87
0.1860	69.81	330.31
0.2510	69.81	329.39
0.4240	69.81	328.66
0.5040	69.81	328.53
0.5660	69.81	328.52
0.7150	69.81	328.60
0.7920	69.81	328.67
0.8600	69.81	329.04
0.9110	69.81	329.70
0.9390	69.81	330.67
0.9660	69.81	332.49
0.9890	69.81	337.70
1.0000	69.81	341.99
0.0000	97.72	350.50
0.0640	97.72	343.56
0.1260	97.72	340.46
0.1870	97.72	338.99
0.3630	97.72	337.57
0.4300	97.72	337.37
0.5690	97.72	337.28
0.7190	97.72	337.42
0.7570	97.72	337.43
0.7740	97.72	337.46
0.8510	97.72	338.06
0.9030	97.72	338.78
0.9590	97.72	342.82
0.9910	97.72	348.82
1.0000	97.72	352.60
0.0000	150.00	361.71
0.0680	150.00	355.17
0.1310	150.00	352.24
0.1950	150.00	350.75
0.2440	150.00	350.02
0.3640	150.00	349.44
0.5160	150.00	349.21
0.5720	150.00	349.23
0.7190	150.00	349.51
0.7990	150.00	350.54
0.9170	150.00	354.19
1.0000	150.00	367.66

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9973	348.85
0.9890	347.55
0.9742	346.55
0.9499	344.75
0.9119	342.75
0.8775	341.45
0.8280	340.05
0.7849	339.35
0.6917	338.55
0.6425	338.35
0.5693	337.95
0.5401	337.85
0.4345	337.65
0.3227	337.75
0.2734	337.85
0.1393	338.75
0.0648	340.55
0.0526	342.15
0.0352	345.75
0.0303	347.65
0.0245	348.65
0.0192	350.15
0.0157	351.35
0.0144	352.75
0.0102	353.45

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0300	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9700	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0300	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9700	0.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 283.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethanol (1) - Liquid	y1[mol/mol] of Ethanol (1) - Vapour
6.266	0.0000	0.0000
8.219	0.0500	0.2498
8.493	0.1000	0.2779
8.619	0.1500	0.2901
8.666	0.2000	0.2939
8.679	0.2500	0.2957
8.679	0.3000	0.2964
8.659	0.3500	0.2964
8.633	0.4000	0.2972
8.599	0.4500	0.2993
8.553	0.5000	0.3017
8.499	0.5500	0.3051
8.439	0.6000	0.3089
8.359	0.6500	0.3158
8.239	0.7000	0.3261
8.059	0.7500	0.3383
7.813	0.8000	0.3532
7.426	0.8500	0.3806
6.753	0.9000	0.4294
5.353	0.9500	0.5617
3.1864	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 293.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethanol (1) - Liquid	y1[mol/mol] of Ethanol (1) - Vapour
10.299	0.0000	0.0000
13.932	0.0500	0.2776
14.385	0.1000	0.3068
14.572	0.1500	0.3194
14.612	0.2000	0.3230
14.625	0.2500	0.3237
14.612	0.3000	0.3258
14.599	0.3500	0.3261
14.585	0.4000	0.3264
14.559	0.4500	0.3269
14.532	0.5000	0.3276
14.492	0.5500	0.3312
14.412	0.6000	0.3359
14.292	0.6500	0.3424
14.092	0.7000	0.3510
13.786	0.7500	0.3675
13.312	0.8000	0.3871
12.566	0.8500	0.4196
11.432	0.9000	0.4752
9.459	0.9500	0.5983
5.94	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 303.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethanol (1) - Liquid	y1[mol/mol] of Ethanol (1) - Vapour
16.231	0.0000	0.0000
22.625	0.0500	0.2923
23.331	0.1000	0.3149
23.585	0.1500	0.3223
23.731	0.2000	0.3275
23.811	0.2500	0.3298
23.851	0.3000	0.3315
23.878	0.3500	0.3339
23.851	0.4000	0.3349
23.811	0.4500	0.3382
23.731	0.5000	0.3422
23.598	0.5500	0.3486
23.425	0.6000	0.3575
23.198	0.6500	0.3673
22.825	0.7000	0.3791
22.385	0.7500	0.3949
21.652	0.8000	0.4163
20.465	0.8500	0.4515
18.598	0.9000	0.5118
15.585	0.9500	0.6330
10.326	1.0000	1.0000

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Isobaric vapor liquid equilibria for ethanol water system containing different ionic liquids at atmospheric pressure
• Solubility of decanedioic acid in binary solvent mixtures
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems