Mixture of Dodecane + 1-Butanol

Datasets

1. Mole fraction (2)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. η - Viscosity, Pa*s (2)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. ρ_l - Mass density, kg/m3 (4)
6. c_sound,fluid - Speed of Sound, m/s (2)
7. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Dodecane (1) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Dodecane (1) - Liquid	Mole fraction of Dodecane (1) - Gas
0.0000	0.0000
0.0070	0.0020
0.0150	0.0040
0.0760	0.0160
0.1330	0.0200
0.2500	0.0270
0.3870	0.0340
0.5100	0.0380
0.6080	0.0430
0.7120	0.0520
0.7860	0.0580
0.8630	0.0850
0.8910	0.1160
0.9340	0.2200
0.9530	0.3810
0.9570	0.4280
1.0000	1.0000

Mole fraction of Dodecane (1) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Dodecane (1) - Liquid	Mole fraction of Dodecane (1) - Gas
0.0000	0.0000
0.0070	0.0020
0.0150	0.0040
0.0760	0.0160
0.1330	0.0200
0.2500	0.0270
0.3870	0.0340
0.5100	0.0380
0.6080	0.0430
0.7120	0.0520
0.7860	0.0580
0.8630	0.0850
0.8910	0.1160
0.9340	0.2200
0.9530	0.3810
0.9570	0.4280
1.0000	1.0000

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
283.15	0.0805	361.08
283.15	0.1902	340.76
283.15	0.2881	321.63
283.15	0.3865	301.93
283.15	0.4410	290.92
283.15	0.4835	282.09
283.15	0.5406	269.83
283.15	0.5885	259.76
283.15	0.6151	253.75
283.15	0.6960	236.27
283.15	0.7959	213.74
283.15	0.9030	189.46
283.15	0.9523	178.05
288.15	0.0805	364.22
288.15	0.1902	344.32
288.15	0.2881	325.39
288.15	0.3865	305.76
288.15	0.4410	294.85
288.15	0.4835	286.04
288.15	0.5406	273.71
288.15	0.5885	263.80
288.15	0.6151	257.68
288.15	0.6960	240.13
288.15	0.7959	217.56
288.15	0.9030	192.97
288.15	0.9523	181.36
298.15	0.0805	370.79
298.15	0.1902	351.89
298.15	0.2881	333.33
298.15	0.3865	313.86
298.15	0.4410	303.08
298.15	0.4835	294.28
298.15	0.5406	281.93
298.15	0.5885	272.13
298.15	0.6151	265.84
298.15	0.6960	248.35
298.15	0.7959	225.46
298.15	0.9030	200.34
298.15	0.9523	188.36
308.15	0.0805	376.59
308.15	0.1902	359.80
308.15	0.2881	341.79
308.15	0.3865	322.51
308.15	0.4410	311.79
308.15	0.4835	303.09
308.15	0.5406	290.73
308.15	0.5885	281.00
308.15	0.6151	274.56
308.15	0.6960	257.05
308.15	0.7959	233.92
308.15	0.9030	208.32
308.15	0.9523	195.95
313.15	0.0805	379.38
313.15	0.1902	363.77
313.15	0.2881	346.13
313.15	0.3865	327.00
313.15	0.4410	316.36
313.15	0.4835	307.67
313.15	0.5406	295.36
313.15	0.5885	285.53
313.15	0.6151	279.13
313.15	0.6960	261.55
313.15	0.7959	238.39
313.15	0.9030	212.48
313.15	0.9523	200.02
318.15	0.0805	382.63
318.15	0.1902	367.77
318.15	0.2881	350.48
318.15	0.3865	331.46
318.15	0.4410	320.93
318.15	0.4835	312.27
318.15	0.5406	300.02
318.15	0.5885	290.20
318.15	0.6151	283.62
318.15	0.6960	266.23
318.15	0.7959	242.97
318.15	0.9030	216.75
318.15	0.9523	204.16

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
283.15	0.0805	361.08
283.15	0.1902	340.76
283.15	0.2881	321.63
283.15	0.3865	301.93
283.15	0.4410	290.92
283.15	0.4835	282.09
283.15	0.5406	269.83
283.15	0.5885	259.76
283.15	0.6151	253.75
283.15	0.6960	236.27
283.15	0.7959	213.74
283.15	0.9030	189.46
283.15	0.9523	178.05
288.15	0.0805	364.22
288.15	0.1902	344.32
288.15	0.2881	325.39
288.15	0.3865	305.76
288.15	0.4410	294.85
288.15	0.4835	286.04
288.15	0.5406	273.71
288.15	0.5885	263.80
288.15	0.6151	257.68
288.15	0.6960	240.13
288.15	0.7959	217.56
288.15	0.9030	192.97
288.15	0.9523	181.36
298.15	0.0805	370.79
298.15	0.1902	351.89
298.15	0.2881	333.33
298.15	0.3865	313.86
298.15	0.4410	303.08
298.15	0.4835	294.28
298.15	0.5406	281.93
298.15	0.5885	272.13
298.15	0.6151	265.84
298.15	0.6960	248.35
298.15	0.7959	225.46
298.15	0.9030	200.34
298.15	0.9523	188.36
308.15	0.0805	376.59
308.15	0.1902	359.80
308.15	0.2881	341.79
308.15	0.3865	322.51
308.15	0.4410	311.79
308.15	0.4835	303.09
308.15	0.5406	290.73
308.15	0.5885	281.00
308.15	0.6151	274.56
308.15	0.6960	257.05
308.15	0.7959	233.92
308.15	0.9030	208.32
308.15	0.9523	195.95
313.15	0.0805	379.38
313.15	0.1902	363.77
313.15	0.2881	346.13
313.15	0.3865	327.00
313.15	0.4410	316.36
313.15	0.4835	307.67
313.15	0.5406	295.36
313.15	0.5885	285.53
313.15	0.6151	279.13
313.15	0.6960	261.55
313.15	0.7959	238.39
313.15	0.9030	212.48
313.15	0.9523	200.02
318.15	0.0805	382.63
318.15	0.1902	367.77
318.15	0.2881	350.48
318.15	0.3865	331.46
318.15	0.4410	320.93
318.15	0.4835	312.27
318.15	0.5406	300.02
318.15	0.5885	290.20
318.15	0.6151	283.62
318.15	0.6960	266.23
318.15	0.7959	242.97
318.15	0.9030	216.75
318.15	0.9523	204.16

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0029
293.15	0.1045	0.0025
293.15	0.2008	0.0022
293.15	0.3002	0.0019
293.15	0.3985	0.0018
293.15	0.4995	0.0016
293.15	0.5978	0.0016
293.15	0.7012	0.0015
293.15	0.7671	0.0015
293.15	0.8773	0.0015
293.15	1.0000	0.0015
298.15	0.0000	0.0026
298.15	0.1045	0.0022
298.15	0.2008	0.0019
298.15	0.3002	0.0017
298.15	0.3985	0.0016
298.15	0.4995	0.0015
298.15	0.5978	0.0014
298.15	0.7012	0.0014
298.15	0.7671	0.0013
298.15	0.8773	0.0013
298.15	1.0000	0.0014
303.15	0.0000	0.0023
303.15	0.1045	0.0019
303.15	0.2008	0.0017
303.15	0.3002	0.0015
303.15	0.3985	0.0014
303.15	0.4995	0.0013
303.15	0.5978	0.0013
303.15	0.7012	0.0012
303.15	0.7671	0.0012
303.15	0.8773	0.0012
303.15	1.0000	0.0013
308.15	0.0000	0.0020
308.15	0.1045	0.0017
308.15	0.2008	0.0015
308.15	0.3002	0.0014
308.15	0.3985	0.0013
308.15	0.4995	0.0012
308.15	0.5978	0.0012
308.15	0.7012	0.0011
308.15	0.7671	0.0011
308.15	0.8773	0.0011
308.15	1.0000	0.0012
313.15	0.0000	0.0018
313.15	0.1045	0.0015
313.15	0.2008	0.0014
313.15	0.3002	0.0013
313.15	0.3985	0.0012
313.15	0.4995	0.0011
313.15	0.5978	0.0011
313.15	0.7012	0.0011
313.15	0.7671	0.0010
313.15	0.8773	0.0010
313.15	1.0000	0.0011
318.15	0.0000	0.0016
318.15	0.1045	0.0014
318.15	0.2008	0.0012
318.15	0.3002	0.0011
318.15	0.3985	0.0011
318.15	0.4995	0.0010
318.15	0.5978	0.0010
318.15	0.7012	0.0010
318.15	0.7671	0.0010
318.15	0.8773	0.0010
318.15	1.0000	0.0010
323.15	0.0000	0.0014
323.15	0.1045	0.0012
323.15	0.2008	0.0011
323.15	0.3002	0.0010
323.15	0.3985	0.0010
323.15	0.4995	0.0009
323.15	0.5978	0.0009
323.15	0.7012	0.0009
323.15	0.7671	0.0009
323.15	0.8773	0.0009
323.15	1.0000	0.0009
328.15	0.0000	0.0013
328.15	0.1045	0.0011
328.15	0.2008	0.0010
328.15	0.3002	0.0009
328.15	0.3985	0.0009
328.15	0.4995	0.0009
328.15	0.5978	0.0009
328.15	0.7012	0.0008
328.15	0.7671	0.0008
328.15	0.8773	0.0008
328.15	1.0000	0.0009
333.15	0.0000	0.0012
333.15	0.1045	0.0010
333.15	0.2008	0.0009
333.15	0.3002	0.0009
333.15	0.3985	0.0008
333.15	0.4995	0.0008
333.15	0.5978	0.0008
333.15	0.7012	0.0008
333.15	0.7671	0.0008
333.15	0.8773	0.0008
333.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0029
293.15	0.1045	0.0025
293.15	0.2008	0.0022
293.15	0.3002	0.0019
293.15	0.3985	0.0018
293.15	0.4995	0.0016
293.15	0.5978	0.0016
293.15	0.7012	0.0015
293.15	0.7671	0.0015
293.15	0.8773	0.0015
293.15	1.0000	0.0015
298.15	0.0000	0.0026
298.15	0.1045	0.0022
298.15	0.2008	0.0019
298.15	0.3002	0.0017
298.15	0.3985	0.0016
298.15	0.4995	0.0015
298.15	0.5978	0.0014
298.15	0.7012	0.0014
298.15	0.7671	0.0013
298.15	0.8773	0.0013
298.15	1.0000	0.0014
303.15	0.0000	0.0023
303.15	0.1045	0.0019
303.15	0.2008	0.0017
303.15	0.3002	0.0015
303.15	0.3985	0.0014
303.15	0.4995	0.0013
303.15	0.5978	0.0013
303.15	0.7012	0.0012
303.15	0.7671	0.0012
303.15	0.8773	0.0012
303.15	1.0000	0.0013
308.15	0.0000	0.0020
308.15	0.1045	0.0017
308.15	0.2008	0.0015
308.15	0.3002	0.0014
308.15	0.3985	0.0013
308.15	0.4995	0.0012
308.15	0.5978	0.0012
308.15	0.7012	0.0011
308.15	0.7671	0.0011
308.15	0.8773	0.0011
308.15	1.0000	0.0012
313.15	0.0000	0.0018
313.15	0.1045	0.0015
313.15	0.2008	0.0014
313.15	0.3002	0.0013
313.15	0.3985	0.0012
313.15	0.4995	0.0011
313.15	0.5978	0.0011
313.15	0.7012	0.0011
313.15	0.7671	0.0010
313.15	0.8773	0.0010
313.15	1.0000	0.0011
318.15	0.0000	0.0016
318.15	0.1045	0.0014
318.15	0.2008	0.0012
318.15	0.3002	0.0011
318.15	0.3985	0.0011
318.15	0.4995	0.0010
318.15	0.5978	0.0010
318.15	0.7012	0.0010
318.15	0.7671	0.0010
318.15	0.8773	0.0010
318.15	1.0000	0.0010
323.15	0.0000	0.0014
323.15	0.1045	0.0012
323.15	0.2008	0.0011
323.15	0.3002	0.0010
323.15	0.3985	0.0010
323.15	0.4995	0.0009
323.15	0.5978	0.0009
323.15	0.7012	0.0009
323.15	0.7671	0.0009
323.15	0.8773	0.0009
323.15	1.0000	0.0009
328.15	0.0000	0.0013
328.15	0.1045	0.0011
328.15	0.2008	0.0010
328.15	0.3002	0.0009
328.15	0.3985	0.0009
328.15	0.4995	0.0009
328.15	0.5978	0.0009
328.15	0.7012	0.0008
328.15	0.7671	0.0008
328.15	0.8773	0.0008
328.15	1.0000	0.0009
333.15	0.0000	0.0012
333.15	0.1045	0.0010
333.15	0.2008	0.0009
333.15	0.3002	0.0009
333.15	0.3985	0.0008
333.15	0.4995	0.0008
333.15	0.5978	0.0008
333.15	0.7012	0.0008
333.15	0.7671	0.0008
333.15	0.8773	0.0008
333.15	1.0000	0.0008

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.06
0.1125	1.61
0.1644	1.76
0.2005	1.82
0.2500	1.89
0.2837	1.93
0.3162	1.97
0.3718	2.02
0.3806	2.03
0.4043	2.04
0.4295	2.06
0.4497	2.07
0.4793	2.09
0.4995	2.10
0.5298	2.12
0.5504	2.12
0.5803	2.14
0.5998	2.15
0.6310	2.17
0.6828	2.19
0.7346	2.22
0.7861	2.25
0.8388	2.30
0.8926	2.34
0.9503	2.42
1.0000	2.50

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.06
0.1125	1.61
0.1644	1.76
0.2005	1.82
0.2500	1.89
0.2837	1.93
0.3162	1.97
0.3718	2.02
0.3806	2.03
0.4043	2.04
0.4295	2.06
0.4497	2.07
0.4793	2.09
0.4995	2.10
0.5298	2.12
0.5504	2.12
0.5803	2.14
0.5998	2.15
0.6310	2.17
0.6828	2.19
0.7346	2.22
0.7861	2.25
0.8388	2.30
0.8926	2.34
0.9503	2.42
1.0000	2.50

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.5
293.15	0.1045	794.67
293.15	0.2008	784.43
293.15	0.3002	776.26
293.15	0.3985	769.8
293.15	0.4995	764.28
293.15	0.5978	759.94
293.15	0.7012	755.99
293.15	0.7671	754.1
293.15	0.8773	751.22
293.15	1.0000	748.83
298.15	0.0000	805.7
298.15	0.1045	790.86
298.15	0.2008	780.62
298.15	0.3002	772.45
298.15	0.3985	765.97
298.15	0.4995	760.49
298.15	0.5978	756.17
298.15	0.7012	752.24
298.15	0.7671	750.38
298.15	0.8773	747.52
298.15	1.0000	745.22
303.15	0.0000	801.87
303.15	0.1045	787.01
303.15	0.2008	776.76
303.15	0.3002	768.59
303.15	0.3985	762.12
303.15	0.4995	756.67
303.15	0.5978	752.37
303.15	0.7012	748.47
303.15	0.7671	746.62
303.15	0.8773	743.81
303.15	1.0000	741.59
308.15	0.0000	798.0
308.15	0.1045	783.13
308.15	0.2008	772.86
308.15	0.3002	764.7
308.15	0.3985	758.24
308.15	0.4995	752.82
308.15	0.5978	748.54
308.15	0.7012	744.67
308.15	0.7671	742.85
308.15	0.8773	740.07
308.15	1.0000	737.95
313.15	0.0000	794.1
313.15	0.1045	779.2
313.15	0.2008	768.93
313.15	0.3002	760.78
313.15	0.3985	754.33
313.15	0.4995	748.93
313.15	0.5978	744.69
313.15	0.7012	740.88
313.15	0.7671	739.06
313.15	0.8773	736.32
313.15	1.0000	734.31
318.15	0.0000	790.15
318.15	0.1045	775.23
318.15	0.2008	764.95
318.15	0.3002	756.81
318.15	0.3985	750.39
318.15	0.4995	745.02
318.15	0.5978	740.81
318.15	0.7012	737.02
318.15	0.7671	735.24
318.15	0.8773	732.55
318.15	1.0000	730.66
323.15	0.0000	786.16
323.15	0.1045	771.21
323.15	0.2008	760.93
323.15	0.3002	752.8
323.15	0.3985	746.41
323.15	0.4995	741.07
323.15	0.5978	736.9
323.15	0.7012	733.15
323.15	0.7671	731.4
323.15	0.8773	728.77
323.15	1.0000	727.0
328.15	0.0000	782.12
328.15	0.1045	767.14
328.15	0.2008	756.86
328.15	0.3002	748.75
328.15	0.3985	742.38
328.15	0.4995	737.08
328.15	0.5978	732.96
328.15	0.7012	729.25
328.15	0.7671	727.53
328.15	0.8773	724.96
328.15	1.0000	723.33
333.15	0.0000	778.01
333.15	0.1045	763.01
333.15	0.2008	752.73
333.15	0.3002	744.64
333.15	0.3985	738.31
333.15	0.4995	733.06
333.15	0.5978	728.98
333.15	0.7012	725.32
333.15	0.7671	723.64
333.15	0.8773	721.13
333.15	1.0000	719.65

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0275	760.0
278.15	0.0805	761.12
278.15	0.1902	763.86
278.15	0.2881	766.84
278.15	0.3865	770.41
278.15	0.4410	772.69
278.15	0.4835	774.61
278.15	0.5885	780.11
278.15	0.6151	781.74
278.15	0.6960	787.13
278.15	0.7959	795.27
278.15	0.9030	806.6
278.15	0.9523	813.2
283.15	0.0275	756.37
283.15	0.0805	757.47
283.15	0.1902	760.19
283.15	0.2881	763.16
283.15	0.3865	766.72
283.15	0.4410	768.97
283.15	0.4835	770.89
283.15	0.5885	776.38
283.15	0.6151	778.04
283.15	0.6960	783.43
283.15	0.7959	791.53
283.15	0.9030	802.88
283.15	0.9523	809.45
288.15	0.0275	752.75
288.15	0.0805	753.82
288.15	0.1902	756.5
288.15	0.2881	759.47
288.15	0.3865	762.98
288.15	0.4410	765.23
288.15	0.4835	767.14
288.15	0.5885	772.65
288.15	0.6151	774.27
288.15	0.6960	779.63
288.15	0.7959	787.76
288.15	0.9030	799.12
288.15	0.9523	805.7
298.15	0.0275	745.49
298.15	0.0805	746.51
298.15	0.1902	749.12
298.15	0.2881	752.04
298.15	0.3865	755.51
298.15	0.4410	757.73
298.15	0.4835	759.62
298.15	0.5885	765.09
298.15	0.6151	766.72
298.15	0.6960	772.04
298.15	0.7959	780.2
298.15	0.9030	791.57
298.15	0.9523	798.15
308.15	0.0275	738.18
308.15	0.0805	739.13
308.15	0.1902	741.67
308.15	0.2881	744.51
308.15	0.3865	747.93
308.15	0.4410	750.12
308.15	0.4835	752.0
308.15	0.5885	757.4
308.15	0.6151	759.03
308.15	0.6960	764.36
308.15	0.7959	772.5
308.15	0.9030	783.88
308.15	0.9523	790.48
313.15	0.0275	734.51
313.15	0.0805	735.41
313.15	0.1902	737.9
313.15	0.2881	740.71
313.15	0.3865	744.09
313.15	0.4410	746.27
313.15	0.4835	748.13
313.15	0.5885	753.51
313.15	0.6151	755.13
313.15	0.6960	760.44
313.15	0.7959	768.57
313.15	0.9030	779.97
313.15	0.9523	786.57
318.15	0.0275	730.8
318.15	0.0805	731.65
318.15	0.1902	734.12
318.15	0.2881	736.86
318.15	0.3865	740.2
318.15	0.4410	742.36
318.15	0.4835	744.23
318.15	0.5885	749.54
318.15	0.6151	751.18
318.15	0.6960	756.46
318.15	0.7959	764.59
318.15	0.9030	775.98
318.15	0.9523	782.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.5
293.15	0.1045	794.67
293.15	0.2008	784.43
293.15	0.3002	776.26
293.15	0.3985	769.8
293.15	0.4995	764.28
293.15	0.5978	759.94
293.15	0.7012	755.99
293.15	0.7671	754.1
293.15	0.8773	751.22
293.15	1.0000	748.83
298.15	0.0000	805.7
298.15	0.1045	790.86
298.15	0.2008	780.62
298.15	0.3002	772.45
298.15	0.3985	765.97
298.15	0.4995	760.49
298.15	0.5978	756.17
298.15	0.7012	752.24
298.15	0.7671	750.38
298.15	0.8773	747.52
298.15	1.0000	745.22
303.15	0.0000	801.87
303.15	0.1045	787.01
303.15	0.2008	776.76
303.15	0.3002	768.59
303.15	0.3985	762.12
303.15	0.4995	756.67
303.15	0.5978	752.37
303.15	0.7012	748.47
303.15	0.7671	746.62
303.15	0.8773	743.81
303.15	1.0000	741.59
308.15	0.0000	798.0
308.15	0.1045	783.13
308.15	0.2008	772.86
308.15	0.3002	764.7
308.15	0.3985	758.24
308.15	0.4995	752.82
308.15	0.5978	748.54
308.15	0.7012	744.67
308.15	0.7671	742.85
308.15	0.8773	740.07
308.15	1.0000	737.95
313.15	0.0000	794.1
313.15	0.1045	779.2
313.15	0.2008	768.93
313.15	0.3002	760.78
313.15	0.3985	754.33
313.15	0.4995	748.93
313.15	0.5978	744.69
313.15	0.7012	740.88
313.15	0.7671	739.06
313.15	0.8773	736.32
313.15	1.0000	734.31
318.15	0.0000	790.15
318.15	0.1045	775.23
318.15	0.2008	764.95
318.15	0.3002	756.81
318.15	0.3985	750.39
318.15	0.4995	745.02
318.15	0.5978	740.81
318.15	0.7012	737.02
318.15	0.7671	735.24
318.15	0.8773	732.55
318.15	1.0000	730.66
323.15	0.0000	786.16
323.15	0.1045	771.21
323.15	0.2008	760.93
323.15	0.3002	752.8
323.15	0.3985	746.41
323.15	0.4995	741.07
323.15	0.5978	736.9
323.15	0.7012	733.15
323.15	0.7671	731.4
323.15	0.8773	728.77
323.15	1.0000	727.0
328.15	0.0000	782.12
328.15	0.1045	767.14
328.15	0.2008	756.86
328.15	0.3002	748.75
328.15	0.3985	742.38
328.15	0.4995	737.08
328.15	0.5978	732.96
328.15	0.7012	729.25
328.15	0.7671	727.53
328.15	0.8773	724.96
328.15	1.0000	723.33
333.15	0.0000	778.01
333.15	0.1045	763.01
333.15	0.2008	752.73
333.15	0.3002	744.64
333.15	0.3985	738.31
333.15	0.4995	733.06
333.15	0.5978	728.98
333.15	0.7012	725.32
333.15	0.7671	723.64
333.15	0.8773	721.13
333.15	1.0000	719.65

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0275	760.0
278.15	0.0805	761.12
278.15	0.1902	763.86
278.15	0.2881	766.84
278.15	0.3865	770.41
278.15	0.4410	772.69
278.15	0.4835	774.61
278.15	0.5885	780.11
278.15	0.6151	781.74
278.15	0.6960	787.13
278.15	0.7959	795.27
278.15	0.9030	806.6
278.15	0.9523	813.2
283.15	0.0275	756.37
283.15	0.0805	757.47
283.15	0.1902	760.19
283.15	0.2881	763.16
283.15	0.3865	766.72
283.15	0.4410	768.97
283.15	0.4835	770.89
283.15	0.5885	776.38
283.15	0.6151	778.04
283.15	0.6960	783.43
283.15	0.7959	791.53
283.15	0.9030	802.88
283.15	0.9523	809.45
288.15	0.0275	752.75
288.15	0.0805	753.82
288.15	0.1902	756.5
288.15	0.2881	759.47
288.15	0.3865	762.98
288.15	0.4410	765.23
288.15	0.4835	767.14
288.15	0.5885	772.65
288.15	0.6151	774.27
288.15	0.6960	779.63
288.15	0.7959	787.76
288.15	0.9030	799.12
288.15	0.9523	805.7
298.15	0.0275	745.49
298.15	0.0805	746.51
298.15	0.1902	749.12
298.15	0.2881	752.04
298.15	0.3865	755.51
298.15	0.4410	757.73
298.15	0.4835	759.62
298.15	0.5885	765.09
298.15	0.6151	766.72
298.15	0.6960	772.04
298.15	0.7959	780.2
298.15	0.9030	791.57
298.15	0.9523	798.15
308.15	0.0275	738.18
308.15	0.0805	739.13
308.15	0.1902	741.67
308.15	0.2881	744.51
308.15	0.3865	747.93
308.15	0.4410	750.12
308.15	0.4835	752.0
308.15	0.5885	757.4
308.15	0.6151	759.03
308.15	0.6960	764.36
308.15	0.7959	772.5
308.15	0.9030	783.88
308.15	0.9523	790.48
313.15	0.0275	734.51
313.15	0.0805	735.41
313.15	0.1902	737.9
313.15	0.2881	740.71
313.15	0.3865	744.09
313.15	0.4410	746.27
313.15	0.4835	748.13
313.15	0.5885	753.51
313.15	0.6151	755.13
313.15	0.6960	760.44
313.15	0.7959	768.57
313.15	0.9030	779.97
313.15	0.9523	786.57
318.15	0.0275	730.8
318.15	0.0805	731.65
318.15	0.1902	734.12
318.15	0.2881	736.86
318.15	0.3865	740.2
318.15	0.4410	742.36
318.15	0.4835	744.23
318.15	0.5885	749.54
318.15	0.6151	751.18
318.15	0.6960	756.46
318.15	0.7959	764.59
318.15	0.9030	775.98
318.15	0.9523	782.6

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0275	1354.43
278.15	0.0805	1351.65
278.15	0.1902	1346.36
278.15	0.2881	1341.97
278.15	0.3865	1337.56
278.15	0.4410	1335.22
278.15	0.4835	1333.14
278.15	0.5885	1328.39
278.15	0.6151	1327.0
278.15	0.6960	1323.29
278.15	0.7959	1318.02
278.15	0.9030	1312.42
278.15	0.9523	1310.21
283.15	0.0275	1334.52
283.15	0.0805	1331.73
283.15	0.1902	1326.51
283.15	0.2881	1322.13
283.15	0.3865	1317.8
283.15	0.4410	1315.38
283.15	0.4835	1313.58
283.15	0.5885	1309.07
283.15	0.6151	1307.93
283.15	0.6960	1304.43
283.15	0.7959	1299.42
283.15	0.9030	1294.4
283.15	0.9523	1292.36
288.15	0.0275	1314.74
288.15	0.0805	1311.88
288.15	0.1902	1306.67
288.15	0.2881	1302.34
288.15	0.3865	1298.07
288.15	0.4410	1295.76
288.15	0.4835	1293.98
288.15	0.5885	1289.78
288.15	0.6151	1288.69
288.15	0.6960	1285.21
288.15	0.7959	1280.87
288.15	0.9030	1276.41
288.15	0.9523	1274.76
298.15	0.0275	1275.72
298.15	0.0805	1272.6
298.15	0.1902	1267.38
298.15	0.2881	1263.17
298.15	0.3865	1259.03
298.15	0.4410	1256.85
298.15	0.4835	1255.23
298.15	0.5885	1251.4
298.15	0.6151	1250.47
298.15	0.6960	1247.52
298.15	0.7959	1244.06
298.15	0.9030	1240.79
298.15	0.9523	1239.77
308.15	0.0275	1237.32
308.15	0.0805	1234.0
308.15	0.1902	1228.68
308.15	0.2881	1224.6
308.15	0.3865	1220.59
308.15	0.4410	1218.52
308.15	0.4835	1217.02
308.15	0.5885	1213.58
308.15	0.6151	1212.77
308.15	0.6960	1210.28
308.15	0.7959	1207.63
308.15	0.9030	1205.58
308.15	0.9523	1205.26
313.15	0.0275	1218.43
313.15	0.0805	1214.93
313.15	0.1902	1209.61
313.15	0.2881	1205.57
313.15	0.3865	1201.58
313.15	0.4410	1199.59
313.15	0.4835	1198.11
313.15	0.5885	1194.84
313.15	0.6151	1194.12
313.15	0.6960	1191.8
313.15	0.7959	1189.59
313.15	0.9030	1188.12
313.15	0.9523	1188.14
318.15	0.0275	1199.74
318.15	0.0805	1196.12
318.15	0.1902	1190.76
318.15	0.2881	1186.7
318.15	0.3865	1182.73
318.15	0.4410	1180.76
318.15	0.4835	1179.44
318.15	0.5885	1176.25
318.15	0.6151	1175.56
318.15	0.6960	1173.49
318.15	0.7959	1171.64
318.15	0.9030	1170.77
318.15	0.9523	1171.1

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0275	1354.43
278.15	0.0805	1351.65
278.15	0.1902	1346.36
278.15	0.2881	1341.97
278.15	0.3865	1337.56
278.15	0.4410	1335.22
278.15	0.4835	1333.14
278.15	0.5885	1328.39
278.15	0.6151	1327.0
278.15	0.6960	1323.29
278.15	0.7959	1318.02
278.15	0.9030	1312.42
278.15	0.9523	1310.21
283.15	0.0275	1334.52
283.15	0.0805	1331.73
283.15	0.1902	1326.51
283.15	0.2881	1322.13
283.15	0.3865	1317.8
283.15	0.4410	1315.38
283.15	0.4835	1313.58
283.15	0.5885	1309.07
283.15	0.6151	1307.93
283.15	0.6960	1304.43
283.15	0.7959	1299.42
283.15	0.9030	1294.4
283.15	0.9523	1292.36
288.15	0.0275	1314.74
288.15	0.0805	1311.88
288.15	0.1902	1306.67
288.15	0.2881	1302.34
288.15	0.3865	1298.07
288.15	0.4410	1295.76
288.15	0.4835	1293.98
288.15	0.5885	1289.78
288.15	0.6151	1288.69
288.15	0.6960	1285.21
288.15	0.7959	1280.87
288.15	0.9030	1276.41
288.15	0.9523	1274.76
298.15	0.0275	1275.72
298.15	0.0805	1272.6
298.15	0.1902	1267.38
298.15	0.2881	1263.17
298.15	0.3865	1259.03
298.15	0.4410	1256.85
298.15	0.4835	1255.23
298.15	0.5885	1251.4
298.15	0.6151	1250.47
298.15	0.6960	1247.52
298.15	0.7959	1244.06
298.15	0.9030	1240.79
298.15	0.9523	1239.77
308.15	0.0275	1237.32
308.15	0.0805	1234.0
308.15	0.1902	1228.68
308.15	0.2881	1224.6
308.15	0.3865	1220.59
308.15	0.4410	1218.52
308.15	0.4835	1217.02
308.15	0.5885	1213.58
308.15	0.6151	1212.77
308.15	0.6960	1210.28
308.15	0.7959	1207.63
308.15	0.9030	1205.58
308.15	0.9523	1205.26
313.15	0.0275	1218.43
313.15	0.0805	1214.93
313.15	0.1902	1209.61
313.15	0.2881	1205.57
313.15	0.3865	1201.58
313.15	0.4410	1199.59
313.15	0.4835	1198.11
313.15	0.5885	1194.84
313.15	0.6151	1194.12
313.15	0.6960	1191.8
313.15	0.7959	1189.59
313.15	0.9030	1188.12
313.15	0.9523	1188.14
318.15	0.0275	1199.74
318.15	0.0805	1196.12
318.15	0.1902	1190.76
318.15	0.2881	1186.7
318.15	0.3865	1182.73
318.15	0.4410	1180.76
318.15	0.4835	1179.44
318.15	0.5885	1176.25
318.15	0.6151	1175.56
318.15	0.6960	1173.49
318.15	0.7959	1171.64
318.15	0.9030	1170.77
318.15	0.9523	1171.1

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Dodecane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	367.10
0.0070	366.10
0.0150	366.50
0.0760	367.10
0.1330	368.20
0.2500	369.60
0.3870	371.30
0.5100	372.70
0.6080	374.40
0.7120	376.60
0.7860	379.20
0.8630	385.90
0.8910	392.60
0.9340	408.20
0.9530	423.50
0.9570	426.60
1.0000	453.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Dodecane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	367.10
0.0070	366.10
0.0150	366.50
0.0760	367.10
0.1330	368.20
0.2500	369.60
0.3870	371.30
0.5100	372.70
0.6080	374.40
0.7120	376.60
0.7860	379.20
0.8630	385.90
0.8910	392.60
0.9340	408.20
0.9530	423.50
0.9570	426.60
1.0000	453.70

Sources

• Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
• Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa