Mixture of 1-Pentanol + Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)-

Datasets

1. Azeotropic composition: mole fraction (6)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. ρ_l - Mass density, kg/m3 (2)
6. T_boil - Boiling temperature at pressure P, K (2)
7. Azeotropic pressure, kPa (2)

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

Temperature, K - Liquid	Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid
328.20	0.7550
333.20	0.7750
338.20	0.7950
343.20	0.8050

Mole fraction of 1-Pentanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of 1-Pentanol (1) - Liquid	Mole fraction of 1-Pentanol (1) - Gas
328.15	0.0000	0.0000
328.15	0.0470	0.4830
328.15	0.1330	0.5530
328.15	0.2730	0.6020
328.15	0.2990	0.6130
328.15	0.3640	0.6280
328.15	0.5030	0.6690
328.15	0.5580	0.6810
328.15	0.6220	0.6960
328.15	0.6690	0.7140
328.15	0.7280	0.7390
328.15	0.7800	0.7630
328.15	0.8330	0.7940
328.15	0.8850	0.8390
328.15	0.9720	0.9120
328.15	0.9940	0.9800
328.15	1.0000	1.0000
333.15	0.0000	0.0000
333.15	0.0470	0.4830
333.15	0.1280	0.5570
333.15	0.2590	0.6090
333.15	0.2910	0.6240
333.15	0.3730	0.6430
333.15	0.4980	0.6770
333.15	0.5490	0.6920
333.15	0.6140	0.7070
333.15	0.6620	0.7250
333.15	0.7280	0.7460
333.15	0.7800	0.7700
333.15	0.8290	0.8000
333.15	0.8850	0.8450
333.15	0.9730	0.9180
333.15	0.9940	0.9780
333.15	1.0000	1.0000
338.15	0.0000	0.0000
338.15	0.0320	0.4630
338.15	0.1130	0.5610
338.15	0.2460	0.6220
338.15	0.2730	0.6340
338.15	0.3430	0.6500
338.15	0.5180	0.6790
338.15	0.5490	0.6930
338.15	0.6060	0.7180
338.15	0.6650	0.7320
338.15	0.7250	0.7530
338.15	0.7770	0.7800
338.15	0.8290	0.8100
338.15	0.8790	0.8450
338.15	0.9720	0.9240
338.15	0.9940	0.9550
338.15	1.0000	1.0000
343.15	0.0000	0.0000
343.15	0.0050	0.3550
343.15	0.1010	0.5580
343.15	0.1410	0.5930
343.15	0.2300	0.6300
343.15	0.2440	0.6380
343.15	0.3090	0.6620
343.15	0.4830	0.6960
343.15	0.5360	0.7070
343.15	0.5930	0.7250
343.15	0.6540	0.7390
343.15	0.7210	0.7670
343.15	0.7770	0.7870
343.15	0.8290	0.8170
343.15	0.8670	0.8420
343.15	0.9500	0.9240
343.15	0.9940	0.9830
343.15	1.0000	1.0000

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Liquid	Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Gas
0.0000	0.0000
0.0260	0.0420
0.0670	0.0880
0.1030	0.1050
0.1590	0.1410
0.2300	0.1850
0.2720	0.2100
0.3580	0.2380
0.4190	0.2630
0.5310	0.2960
0.6480	0.3310
0.7890	0.3860
0.8550	0.4320
0.9150	0.4940
0.9400	0.5730
0.9620	0.6760
0.9760	0.8500
1.0000	1.0000

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

Temperature, K - Liquid	Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid
328.20	0.7550
333.20	0.7750
338.20	0.7950
343.20	0.8050

Mole fraction of 1-Pentanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of 1-Pentanol (1) - Liquid	Mole fraction of 1-Pentanol (1) - Gas
328.15	0.0000	0.0000
328.15	0.0470	0.4830
328.15	0.1330	0.5530
328.15	0.2730	0.6020
328.15	0.2990	0.6130
328.15	0.3640	0.6280
328.15	0.5030	0.6690
328.15	0.5580	0.6810
328.15	0.6220	0.6960
328.15	0.6690	0.7140
328.15	0.7280	0.7390
328.15	0.7800	0.7630
328.15	0.8330	0.7940
328.15	0.8850	0.8390
328.15	0.9720	0.9120
328.15	0.9940	0.9800
328.15	1.0000	1.0000
333.15	0.0000	0.0000
333.15	0.0470	0.4830
333.15	0.1280	0.5570
333.15	0.2590	0.6090
333.15	0.2910	0.6240
333.15	0.3730	0.6430
333.15	0.4980	0.6770
333.15	0.5490	0.6920
333.15	0.6140	0.7070
333.15	0.6620	0.7250
333.15	0.7280	0.7460
333.15	0.7800	0.7700
333.15	0.8290	0.8000
333.15	0.8850	0.8450
333.15	0.9730	0.9180
333.15	0.9940	0.9780
333.15	1.0000	1.0000
338.15	0.0000	0.0000
338.15	0.0320	0.4630
338.15	0.1130	0.5610
338.15	0.2460	0.6220
338.15	0.2730	0.6340
338.15	0.3430	0.6500
338.15	0.5180	0.6790
338.15	0.5490	0.6930
338.15	0.6060	0.7180
338.15	0.6650	0.7320
338.15	0.7250	0.7530
338.15	0.7770	0.7800
338.15	0.8290	0.8100
338.15	0.8790	0.8450
338.15	0.9720	0.9240
338.15	0.9940	0.9550
338.15	1.0000	1.0000
343.15	0.0000	0.0000
343.15	0.0050	0.3550
343.15	0.1010	0.5580
343.15	0.1410	0.5930
343.15	0.2300	0.6300
343.15	0.2440	0.6380
343.15	0.3090	0.6620
343.15	0.4830	0.6960
343.15	0.5360	0.7070
343.15	0.5930	0.7250
343.15	0.6540	0.7390
343.15	0.7210	0.7670
343.15	0.7770	0.7870
343.15	0.8290	0.8170
343.15	0.8670	0.8420
343.15	0.9500	0.9240
343.15	0.9940	0.9830
343.15	1.0000	1.0000

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Liquid	Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Gas
0.0000	0.0000
0.0260	0.0420
0.0670	0.0880
0.1030	0.1050
0.1590	0.1410
0.2300	0.1850
0.2720	0.2100
0.3580	0.2380
0.4190	0.2630
0.5310	0.2960
0.6480	0.3310
0.7890	0.3860
0.8550	0.4320
0.9150	0.4940
0.9400	0.5730
0.9620	0.6760
0.9760	0.8500
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0009
293.15	0.0920	0.0009
293.15	0.1644	0.0010
293.15	0.2748	0.0011
293.15	0.3592	0.0012
293.15	0.4565	0.0013
293.15	0.5542	0.0016
293.15	0.6068	0.0017
293.15	0.6470	0.0019
293.15	0.7365	0.0022
293.15	0.8234	0.0027
293.15	0.9105	0.0033
293.15	1.0000	0.0040
303.15	0.0000	0.0008
303.15	0.0920	0.0008
303.15	0.1644	0.0008
303.15	0.2748	0.0009
303.15	0.3592	0.0010
303.15	0.4565	0.0011
303.15	0.5542	0.0013
303.15	0.6068	0.0014
303.15	0.6470	0.0015
303.15	0.7365	0.0017
303.15	0.8234	0.0021
303.15	0.9105	0.0025
303.15	1.0000	0.0030
313.15	0.0000	0.0007
313.15	0.0920	0.0007
313.15	0.1644	0.0007
313.15	0.2748	0.0008
313.15	0.3592	0.0009
313.15	0.4565	0.0009
313.15	0.5542	0.0011
313.15	0.6068	0.0011
313.15	0.6470	0.0012
313.15	0.7365	0.0014
313.15	0.8234	0.0016
313.15	0.9105	0.0019
313.15	1.0000	0.0023
323.15	0.0000	0.0006
323.15	0.0920	0.0006
323.15	0.1644	0.0007
323.15	0.2748	0.0007
323.15	0.3592	0.0007
323.15	0.4565	0.0008
323.15	0.5542	0.0009
323.15	0.6068	0.0009
323.15	0.6470	0.0010
323.15	0.7365	0.0011
323.15	0.8234	0.0013
323.15	0.9105	0.0015
323.15	1.0000	0.0018
333.15	0.0000	0.0006
333.15	0.0920	0.0006
333.15	0.1644	0.0006
333.15	0.2748	0.0006
333.15	0.3592	0.0006
333.15	0.4565	0.0007
333.15	0.5542	0.0008
333.15	0.6068	0.0008
333.15	0.6470	0.0008
333.15	0.7365	0.0009
333.15	0.8234	0.0011
333.15	0.9105	0.0012
333.15	1.0000	0.0014
343.15	0.0000	0.0005
343.15	0.0920	0.0005
343.15	0.1644	0.0005
343.15	0.2748	0.0005
343.15	0.3592	0.0006
343.15	0.4565	0.0006
343.15	0.5542	0.0007
343.15	0.6068	0.0007
343.15	0.6470	0.0007
343.15	0.7365	0.0008
343.15	0.8234	0.0009
343.15	0.9105	0.0010
343.15	1.0000	0.0011
353.15	0.0000	0.0005
353.15	0.0920	0.0005
353.15	0.1644	0.0005
353.15	0.2748	0.0005
353.15	0.3592	0.0005
353.15	0.4565	0.0005
353.15	0.5542	0.0006
353.15	0.6068	0.0006
353.15	0.6470	0.0006
353.15	0.7365	0.0007
353.15	0.8234	0.0007
353.15	0.9105	0.0008
353.15	1.0000	0.0009
363.15	0.0000	0.0004
363.15	0.0920	0.0004
363.15	0.1644	0.0004
363.15	0.2748	0.0004
363.15	0.3592	0.0004
363.15	0.4565	0.0005
363.15	0.5542	0.0005
363.15	0.6068	0.0005
363.15	0.6470	0.0005
363.15	0.7365	0.0006
363.15	0.8234	0.0006
363.15	0.9105	0.0007
363.15	1.0000	0.0008
373.15	0.0000	0.0004
373.15	0.0920	0.0004
373.15	0.1644	0.0004
373.15	0.2748	0.0004
373.15	0.3592	0.0004
373.15	0.4565	0.0004
373.15	0.5542	0.0004
373.15	0.6068	0.0005
373.15	0.6470	0.0005
373.15	0.7365	0.0005
373.15	0.8234	0.0005
373.15	0.9105	0.0006
373.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0009
293.15	0.0920	0.0009
293.15	0.1644	0.0010
293.15	0.2748	0.0011
293.15	0.3592	0.0012
293.15	0.4565	0.0013
293.15	0.5542	0.0016
293.15	0.6068	0.0017
293.15	0.6470	0.0019
293.15	0.7365	0.0022
293.15	0.8234	0.0027
293.15	0.9105	0.0033
293.15	1.0000	0.0040
303.15	0.0000	0.0008
303.15	0.0920	0.0008
303.15	0.1644	0.0008
303.15	0.2748	0.0009
303.15	0.3592	0.0010
303.15	0.4565	0.0011
303.15	0.5542	0.0013
303.15	0.6068	0.0014
303.15	0.6470	0.0015
303.15	0.7365	0.0017
303.15	0.8234	0.0021
303.15	0.9105	0.0025
303.15	1.0000	0.0030
313.15	0.0000	0.0007
313.15	0.0920	0.0007
313.15	0.1644	0.0007
313.15	0.2748	0.0008
313.15	0.3592	0.0009
313.15	0.4565	0.0009
313.15	0.5542	0.0011
313.15	0.6068	0.0011
313.15	0.6470	0.0012
313.15	0.7365	0.0014
313.15	0.8234	0.0016
313.15	0.9105	0.0019
313.15	1.0000	0.0023
323.15	0.0000	0.0006
323.15	0.0920	0.0006
323.15	0.1644	0.0007
323.15	0.2748	0.0007
323.15	0.3592	0.0007
323.15	0.4565	0.0008
323.15	0.5542	0.0009
323.15	0.6068	0.0009
323.15	0.6470	0.0010
323.15	0.7365	0.0011
323.15	0.8234	0.0013
323.15	0.9105	0.0015
323.15	1.0000	0.0018
333.15	0.0000	0.0006
333.15	0.0920	0.0006
333.15	0.1644	0.0006
333.15	0.2748	0.0006
333.15	0.3592	0.0006
333.15	0.4565	0.0007
333.15	0.5542	0.0008
333.15	0.6068	0.0008
333.15	0.6470	0.0008
333.15	0.7365	0.0009
333.15	0.8234	0.0011
333.15	0.9105	0.0012
333.15	1.0000	0.0014
343.15	0.0000	0.0005
343.15	0.0920	0.0005
343.15	0.1644	0.0005
343.15	0.2748	0.0005
343.15	0.3592	0.0006
343.15	0.4565	0.0006
343.15	0.5542	0.0007
343.15	0.6068	0.0007
343.15	0.6470	0.0007
343.15	0.7365	0.0008
343.15	0.8234	0.0009
343.15	0.9105	0.0010
343.15	1.0000	0.0011
353.15	0.0000	0.0005
353.15	0.0920	0.0005
353.15	0.1644	0.0005
353.15	0.2748	0.0005
353.15	0.3592	0.0005
353.15	0.4565	0.0005
353.15	0.5542	0.0006
353.15	0.6068	0.0006
353.15	0.6470	0.0006
353.15	0.7365	0.0007
353.15	0.8234	0.0007
353.15	0.9105	0.0008
353.15	1.0000	0.0009
363.15	0.0000	0.0004
363.15	0.0920	0.0004
363.15	0.1644	0.0004
363.15	0.2748	0.0004
363.15	0.3592	0.0004
363.15	0.4565	0.0005
363.15	0.5542	0.0005
363.15	0.6068	0.0005
363.15	0.6470	0.0005
363.15	0.7365	0.0006
363.15	0.8234	0.0006
363.15	0.9105	0.0007
363.15	1.0000	0.0008
373.15	0.0000	0.0004
373.15	0.0920	0.0004
373.15	0.1644	0.0004
373.15	0.2748	0.0004
373.15	0.3592	0.0004
373.15	0.4565	0.0004
373.15	0.5542	0.0004
373.15	0.6068	0.0005
373.15	0.6470	0.0005
373.15	0.7365	0.0005
373.15	0.8234	0.0005
373.15	0.9105	0.0006
373.15	1.0000	0.0006

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303 (Liquid)

Mole fraction of 1-Pentanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0230	0.2340
0.0580	0.4560
0.1080	0.6560
0.1670	0.6510
0.1760	0.6840
0.2340	0.7820
0.3470	0.8420
0.4600	0.8580
0.5470	0.8150
0.6020	0.7220
0.6780	0.6390
0.7280	0.5320
0.8280	0.4390
0.8570	0.3460
0.9540	0.1840
0.9610	0.1000
1.0000	0.0000

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303 (Liquid)

Mole fraction of 1-Pentanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0230	0.2340
0.0580	0.4560
0.1080	0.6560
0.1670	0.6510
0.1760	0.6840
0.2340	0.7820
0.3470	0.8420
0.4600	0.8580
0.5470	0.8150
0.6020	0.7220
0.6780	0.6390
0.7280	0.5320
0.8280	0.4390
0.8570	0.3460
0.9540	0.1840
0.9610	0.1000
1.0000	0.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
328.15	0.0000	1.08
328.15	0.0470	1.90
328.15	0.1330	2.14
328.15	0.2730	2.31
328.15	0.2990	2.33
328.15	0.3640	2.38
328.15	0.5030	2.43
328.15	0.5580	2.46
328.15	0.6220	2.48
328.15	0.6690	2.52
328.15	0.7280	2.53
328.15	0.7800	2.52
328.15	0.8330	2.50
328.15	0.8850	2.47
328.15	0.9720	2.37
328.15	0.9940	2.35
328.15	1.0000	2.30
333.15	0.0000	1.44
333.15	0.0470	2.50
333.15	0.1280	2.90
333.15	0.2590	3.10
333.15	0.2910	3.14
333.15	0.3730	3.22
333.15	0.4980	3.28
333.15	0.5490	3.30
333.15	0.6140	3.32
333.15	0.6620	3.38
333.15	0.7280	3.40
333.15	0.7800	3.39
333.15	0.8290	3.36
333.15	0.8850	3.32
333.15	0.9730	3.22
333.15	0.9940	3.20
333.15	1.0000	3.13
338.15	0.0000	1.90
338.15	0.0320	3.33
338.15	0.1130	3.72
338.15	0.2460	4.11
338.15	0.2730	4.18
338.15	0.3430	4.26
338.15	0.5180	4.38
338.15	0.5490	4.41
338.15	0.6060	4.42
338.15	0.6650	4.43
338.15	0.7250	4.48
338.15	0.7770	4.48
338.15	0.8290	4.47
338.15	0.8790	4.45
338.15	0.9720	4.30
338.15	0.9940	4.29
338.15	1.0000	4.19
343.15	0.0000	2.44
343.15	0.0050	3.82
343.15	0.1010	4.67
343.15	0.1410	5.01
343.15	0.2300	5.31
343.15	0.2440	5.34
343.15	0.3090	5.48
343.15	0.4830	5.72
343.15	0.5360	5.78
343.15	0.5930	5.81
343.15	0.6540	5.84
343.15	0.7210	5.87
343.15	0.7770	5.89
343.15	0.8290	5.86
343.15	0.8670	5.80
343.15	0.9500	5.69
343.15	0.9940	5.60
343.15	1.0000	5.56

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
328.15	0.0000	1.08
328.15	0.0470	1.90
328.15	0.1330	2.14
328.15	0.2730	2.31
328.15	0.2990	2.33
328.15	0.3640	2.38
328.15	0.5030	2.43
328.15	0.5580	2.46
328.15	0.6220	2.48
328.15	0.6690	2.52
328.15	0.7280	2.53
328.15	0.7800	2.52
328.15	0.8330	2.50
328.15	0.8850	2.47
328.15	0.9720	2.37
328.15	0.9940	2.35
328.15	1.0000	2.30
333.15	0.0000	1.44
333.15	0.0470	2.50
333.15	0.1280	2.90
333.15	0.2590	3.10
333.15	0.2910	3.14
333.15	0.3730	3.22
333.15	0.4980	3.28
333.15	0.5490	3.30
333.15	0.6140	3.32
333.15	0.6620	3.38
333.15	0.7280	3.40
333.15	0.7800	3.39
333.15	0.8290	3.36
333.15	0.8850	3.32
333.15	0.9730	3.22
333.15	0.9940	3.20
333.15	1.0000	3.13
338.15	0.0000	1.90
338.15	0.0320	3.33
338.15	0.1130	3.72
338.15	0.2460	4.11
338.15	0.2730	4.18
338.15	0.3430	4.26
338.15	0.5180	4.38
338.15	0.5490	4.41
338.15	0.6060	4.42
338.15	0.6650	4.43
338.15	0.7250	4.48
338.15	0.7770	4.48
338.15	0.8290	4.47
338.15	0.8790	4.45
338.15	0.9720	4.30
338.15	0.9940	4.29
338.15	1.0000	4.19
343.15	0.0000	2.44
343.15	0.0050	3.82
343.15	0.1010	4.67
343.15	0.1410	5.01
343.15	0.2300	5.31
343.15	0.2440	5.34
343.15	0.3090	5.48
343.15	0.4830	5.72
343.15	0.5360	5.78
343.15	0.5930	5.81
343.15	0.6540	5.84
343.15	0.7210	5.87
343.15	0.7770	5.89
343.15	0.8290	5.86
343.15	0.8670	5.80
343.15	0.9500	5.69
343.15	0.9940	5.60
343.15	1.0000	5.56

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	841.5
293.15	0.0920	839.4
293.15	0.1644	837.8
293.15	0.2748	835.4
293.15	0.3592	833.5
293.15	0.4565	831.2
293.15	0.5542	828.8
293.15	0.6068	827.4
293.15	0.6470	826.4
293.15	0.7365	823.8
293.15	0.8234	821.1
293.15	0.9105	818.1
293.15	1.0000	814.7
303.15	0.0000	833.6
303.15	0.0920	831.4
303.15	0.1644	829.8
303.15	0.2748	827.4
303.15	0.3592	825.4
303.15	0.4565	823.2
303.15	0.5542	820.8
303.15	0.6068	819.5
303.15	0.6470	818.4
303.15	0.7365	816.0
303.15	0.8234	813.4
303.15	0.9105	810.5
303.15	1.0000	807.2
313.15	0.0000	825.8
313.15	0.0920	823.4
313.15	0.1644	821.8
313.15	0.2748	819.4
313.15	0.3592	817.4
313.15	0.4565	815.2
313.15	0.5542	812.9
313.15	0.6068	811.6
313.15	0.6470	810.6
313.15	0.7365	808.2
313.15	0.8234	805.8
313.15	0.9105	803.0
313.15	1.0000	799.8
323.15	0.0000	817.9
323.15	0.0920	815.4
323.15	0.1644	813.7
323.15	0.2748	811.3
323.15	0.3592	809.3
323.15	0.4565	807.1
323.15	0.5542	804.8
323.15	0.6068	803.5
323.15	0.6470	802.5
323.15	0.7365	800.2
323.15	0.8234	797.9
323.15	0.9105	795.3
323.15	1.0000	792.2
333.15	0.0000	809.9
333.15	0.0920	807.3
333.15	0.1644	805.5
333.15	0.2748	803.0
333.15	0.3592	801.0
333.15	0.4565	798.8
333.15	0.5542	796.5
333.15	0.6068	795.2
333.15	0.6470	794.2
333.15	0.7365	792.2
333.15	0.8234	789.8
333.15	0.9105	787.3
333.15	1.0000	784.3
343.15	0.0000	801.9
343.15	0.0920	799.2
343.15	0.1644	797.2
343.15	0.2748	794.6
343.15	0.3592	792.6
343.15	0.4565	790.4
343.15	0.5542	788.2
343.15	0.6068	787.0
343.15	0.6470	786.0
343.15	0.7365	783.7
343.15	0.8234	781.5
343.15	0.9105	779.1
343.15	1.0000	776.3
353.15	0.0000	793.6
353.15	0.0920	790.8
353.15	0.1644	788.9
353.15	0.2748	786.2
353.15	0.3592	784.2
353.15	0.4565	781.9
353.15	0.5542	779.5
353.15	0.6068	778.4
353.15	0.6470	777.4
353.15	0.7365	775.2
353.15	0.8234	773.1
353.15	0.9105	770.6
353.15	1.0000	768.0
363.15	0.0000	785.4
363.15	0.0920	782.5
363.15	0.1644	780.4
363.15	0.2748	777.7
363.15	0.3592	775.6
363.15	0.4565	773.2
363.15	0.5542	770.9
363.15	0.6068	769.6
363.15	0.6470	768.6
363.15	0.7365	766.5
363.15	0.8234	764.4
363.15	0.9105	762.0
363.15	1.0000	759.5
373.15	0.0000	777.1
373.15	0.0920	774.3
373.15	0.1644	771.9
373.15	0.2748	769.0
373.15	0.3592	766.9
373.15	0.4565	764.4
373.15	0.5542	762.0
373.15	0.6068	760.7
373.15	0.6470	759.7
373.15	0.7365	757.7
373.15	0.8234	755.7
373.15	0.9105	753.1
373.15	1.0000	750.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	841.5
293.15	0.0920	839.4
293.15	0.1644	837.8
293.15	0.2748	835.4
293.15	0.3592	833.5
293.15	0.4565	831.2
293.15	0.5542	828.8
293.15	0.6068	827.4
293.15	0.6470	826.4
293.15	0.7365	823.8
293.15	0.8234	821.1
293.15	0.9105	818.1
293.15	1.0000	814.7
303.15	0.0000	833.6
303.15	0.0920	831.4
303.15	0.1644	829.8
303.15	0.2748	827.4
303.15	0.3592	825.4
303.15	0.4565	823.2
303.15	0.5542	820.8
303.15	0.6068	819.5
303.15	0.6470	818.4
303.15	0.7365	816.0
303.15	0.8234	813.4
303.15	0.9105	810.5
303.15	1.0000	807.2
313.15	0.0000	825.8
313.15	0.0920	823.4
313.15	0.1644	821.8
313.15	0.2748	819.4
313.15	0.3592	817.4
313.15	0.4565	815.2
313.15	0.5542	812.9
313.15	0.6068	811.6
313.15	0.6470	810.6
313.15	0.7365	808.2
313.15	0.8234	805.8
313.15	0.9105	803.0
313.15	1.0000	799.8
323.15	0.0000	817.9
323.15	0.0920	815.4
323.15	0.1644	813.7
323.15	0.2748	811.3
323.15	0.3592	809.3
323.15	0.4565	807.1
323.15	0.5542	804.8
323.15	0.6068	803.5
323.15	0.6470	802.5
323.15	0.7365	800.2
323.15	0.8234	797.9
323.15	0.9105	795.3
323.15	1.0000	792.2
333.15	0.0000	809.9
333.15	0.0920	807.3
333.15	0.1644	805.5
333.15	0.2748	803.0
333.15	0.3592	801.0
333.15	0.4565	798.8
333.15	0.5542	796.5
333.15	0.6068	795.2
333.15	0.6470	794.2
333.15	0.7365	792.2
333.15	0.8234	789.8
333.15	0.9105	787.3
333.15	1.0000	784.3
343.15	0.0000	801.9
343.15	0.0920	799.2
343.15	0.1644	797.2
343.15	0.2748	794.6
343.15	0.3592	792.6
343.15	0.4565	790.4
343.15	0.5542	788.2
343.15	0.6068	787.0
343.15	0.6470	786.0
343.15	0.7365	783.7
343.15	0.8234	781.5
343.15	0.9105	779.1
343.15	1.0000	776.3
353.15	0.0000	793.6
353.15	0.0920	790.8
353.15	0.1644	788.9
353.15	0.2748	786.2
353.15	0.3592	784.2
353.15	0.4565	781.9
353.15	0.5542	779.5
353.15	0.6068	778.4
353.15	0.6470	777.4
353.15	0.7365	775.2
353.15	0.8234	773.1
353.15	0.9105	770.6
353.15	1.0000	768.0
363.15	0.0000	785.4
363.15	0.0920	782.5
363.15	0.1644	780.4
363.15	0.2748	777.7
363.15	0.3592	775.6
363.15	0.4565	773.2
363.15	0.5542	770.9
363.15	0.6068	769.6
363.15	0.6470	768.6
363.15	0.7365	766.5
363.15	0.8234	764.4
363.15	0.9105	762.0
363.15	1.0000	759.5
373.15	0.0000	777.1
373.15	0.0920	774.3
373.15	0.1644	771.9
373.15	0.2748	769.0
373.15	0.3592	766.9
373.15	0.4565	764.4
373.15	0.5542	762.0
373.15	0.6068	760.7
373.15	0.6470	759.7
373.15	0.7365	757.7
373.15	0.8234	755.7
373.15	0.9105	753.1
373.15	1.0000	750.6

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	384.70
0.0260	384.70
0.0670	384.80
0.1030	384.80
0.1590	384.90
0.2300	385.00
0.2720	385.50
0.3580	385.80
0.4190	386.30
0.5310	387.50
0.6480	389.20
0.7890	392.10
0.8550	394.30
0.9150	397.10
0.9400	401.30
0.9620	405.10
0.9760	411.20
1.0000	415.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	384.70
0.0260	384.70
0.0670	384.80
0.1030	384.80
0.1590	384.90
0.2300	385.00
0.2720	385.50
0.3580	385.80
0.4190	386.30
0.5310	387.50
0.6480	389.20
0.7890	392.10
0.8550	394.30
0.9150	397.10
0.9400	401.30
0.9620	405.10
0.9760	411.20
1.0000	415.70

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
328.20	2.50
333.20	3.40
338.20	4.50
343.20	5.90

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
328.20	2.50
333.20	3.40
338.20	4.50
343.20	5.90

Sources

• Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa