Mixture of 1-Butanol + Eucalyptol

Datasets

1. P_vap - Vapor or sublimation pressure, kPa
2. n₀ - Refractive index (Na D-line)
3. ρ_l - Mass density, kg/m3
4. c_sound,fluid - Speed of Sound, m/s

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
278.15	0.0771	0.20
278.15	0.1369	0.20
278.15	0.1976	0.19
278.15	0.2736	0.18
278.15	0.3487	0.18
278.15	0.4857	0.16
278.15	0.5995	0.15
278.15	0.6508	0.15
278.15	0.6810	0.14
278.15	0.7741	0.13
278.15	0.8852	0.11
278.15	0.9346	0.10
283.15	0.0771	0.31
283.15	0.1369	0.29
283.15	0.1976	0.30
283.15	0.2736	0.27
283.15	0.3487	0.26
283.15	0.4857	0.24
283.15	0.5995	0.22
283.15	0.6508	0.21
283.15	0.6810	0.20
283.15	0.7741	0.18
283.15	0.8852	0.15
283.15	0.9346	0.13
288.15	0.0771	0.44
288.15	0.1369	0.43
288.15	0.1976	0.42
288.15	0.2736	0.39
288.15	0.3487	0.38
288.15	0.4857	0.34
288.15	0.5995	0.35
288.15	0.6508	0.31
288.15	0.6810	0.28
288.15	0.7741	0.26
288.15	0.8852	0.22
288.15	0.9346	0.18
293.15	0.0771	0.64
293.15	0.1369	0.64
293.15	0.1976	0.59
293.15	0.2736	0.57
293.15	0.3487	0.55
293.15	0.4857	0.51
293.15	0.5995	0.48
293.15	0.6508	0.44
293.15	0.6810	0.43
293.15	0.7741	0.38
293.15	0.8852	0.30
293.15	0.9346	0.25
298.15	0.0771	0.91
298.15	0.1369	0.90
298.15	0.1976	0.84
298.15	0.2736	0.81
298.15	0.3487	0.79
298.15	0.4857	0.72
298.15	0.5995	0.67
298.15	0.6508	0.64
298.15	0.6811	0.60
298.15	0.7742	0.53
298.15	0.8852	0.43
298.15	0.9346	0.36
303.15	0.0771	1.28
303.15	0.1369	1.25
303.15	0.1976	1.19
303.15	0.2736	1.14
303.15	0.3487	1.09
303.15	0.4858	1.00
303.15	0.5996	0.91
303.15	0.6509	0.88
303.15	0.6811	0.84
303.15	0.7742	0.74
303.15	0.8852	0.60
303.15	0.9346	0.48
308.15	0.0771	1.77
308.15	0.1369	1.73
308.15	0.1976	1.65
308.15	0.2736	1.60
308.15	0.3487	1.52
308.15	0.4858	1.38
308.15	0.5996	1.26
308.15	0.6509	1.21
308.15	0.6811	1.16
308.15	0.7742	1.03
308.15	0.8853	0.81
308.15	0.9347	0.68
313.15	0.0771	2.44
313.15	0.1369	2.38
313.15	0.1976	2.28
313.15	0.2737	2.17
313.15	0.3488	2.08
313.15	0.4858	1.89
313.15	0.5996	1.72
313.15	0.6509	1.64
313.15	0.6812	1.58
313.15	0.7743	1.37
313.15	0.8853	1.10
313.15	0.9347	0.92
318.15	0.0771	3.30
318.15	0.1370	3.17
318.15	0.1977	3.09
318.15	0.2737	2.94
318.15	0.3488	2.81
318.15	0.4859	2.56
318.15	0.5997	2.33
318.15	0.6510	2.21
318.15	0.6812	2.12
318.15	0.7743	1.86
318.15	0.8853	1.44
318.15	0.9347	1.21
323.15	0.0771	4.39
323.15	0.1370	4.25
323.15	0.1977	4.08
323.15	0.2737	3.89
323.15	0.3488	3.71
323.15	0.4860	3.36
323.15	0.5997	3.06
323.15	0.6511	2.92
323.15	0.6813	2.83
323.15	0.7744	2.45
323.15	0.8854	1.92
323.15	0.9348	1.60

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.3973
298.15	0.0494	1.4028
298.15	0.0997	1.4078
298.15	0.2007	1.4169
298.15	0.2916	1.4238
298.15	0.3893	1.4302
298.15	0.4970	1.4363
298.15	0.5913	1.441
298.15	0.6964	1.4455
298.15	0.7977	1.4493
298.15	0.9089	1.4528
298.15	0.9629	1.4536
298.15	1.0000	1.4553
313.15	0.0000	1.3911
313.15	0.0494	1.3965
313.15	0.0997	1.4015
313.15	0.2007	1.4105
313.15	0.2916	1.4173
313.15	0.3893	1.4237
313.15	0.4970	1.4297
313.15	0.5913	1.4343
313.15	0.6964	1.4387
313.15	0.7977	1.4424
313.15	0.9089	1.4459
313.15	0.9629	1.4466
313.15	1.0000	1.4483

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	805.73
298.15	0.0494	817.0
298.15	0.0997	827.27
298.15	0.2007	845.31
298.15	0.2916	859.07
298.15	0.3893	871.88
298.15	0.4970	883.91
298.15	0.5913	892.98
298.15	0.6964	901.77
298.15	0.7977	909.07
298.15	0.9089	915.78
298.15	0.9629	918.54
298.15	1.0000	920.24
313.15	0.0000	794.12
313.15	0.0494	805.25
313.15	0.0997	815.51
313.15	0.2007	833.33
313.15	0.2916	846.89
313.15	0.3893	859.45
313.15	0.4970	871.33
313.15	0.5913	880.29
313.15	0.6964	888.96
313.15	0.7977	896.17
313.15	0.9089	902.85
313.15	0.9629	905.6
313.15	1.0000	907.29

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1239.7
298.15	0.0494	1248.2
298.15	0.0997	1254.8
298.15	0.2007	1264.2
298.15	0.2916	1270.1
298.15	0.3893	1275.1
298.15	0.4970	1278.9
298.15	0.5913	1281.0
298.15	0.6964	1282.6
298.15	0.7977	1283.8
298.15	0.9089	1282.5
298.15	0.9629	1281.3
298.15	1.0000	1280.1
313.15	0.0000	1189.8
313.15	0.0494	1197.2
313.15	0.0997	1203.4
313.15	0.2007	1211.4
313.15	0.2916	1216.1
313.15	0.3893	1220.3
313.15	0.4970	1223.3
313.15	0.5913	1224.8
313.15	0.6964	1226.0
313.15	0.7977	1226.0
313.15	0.9089	1223.9
313.15	0.9629	1222.6
313.15	1.0000	1221.1

Sources

• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Isothermal Vapor-Liquid Equilibrium of (1-Butanol + 1,8-Cineole) at 10 Temperatures between (278.15 and 323.15) K

Note: These property values are available through the Cheméo API. A free account gives you an access key.