Mixture of Ethanol + Eucalyptol

Datasets

1. Mole fraction (2)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (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 Eucalyptol (2) [ref]

Fixed		Measured
Mole fraction of Eucalyptol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Eucalyptol (2) - Gas
0.0047	33.33	0.0006
0.0500	33.33	0.0056
0.0719	33.33	0.0071
0.1193	33.33	0.0096
0.1816	33.33	0.0126
0.2161	33.33	0.0142
0.2901	33.33	0.0178
0.3814	33.33	0.0225
0.4586	33.33	0.0290
0.5952	33.33	0.0407
0.7105	33.33	0.0545
0.8154	33.33	0.0886
0.8429	33.33	0.1006
0.8940	33.33	0.1418
0.9190	33.33	0.1753
0.9460	33.33	0.2493
0.9773	33.33	0.4595
0.9856	33.33	0.5862
0.9959	33.33	0.8396
0.0097	66.66	0.0010
0.0266	66.66	0.0025
0.1011	66.66	0.0088
0.1736	66.66	0.0137
0.2898	66.66	0.0201
0.3823	66.66	0.0263
0.5073	66.66	0.0367
0.5933	66.66	0.0478
0.6947	66.66	0.0640
0.7858	66.66	0.0850
0.8244	66.66	0.0968
0.9043	66.66	0.1566
0.9320	66.66	0.2045
0.9659	66.66	0.3543
0.9805	66.66	0.4862
0.9939	66.66	0.7675
0.9979	66.66	0.9049
0.0154	101.33	0.0017
0.0337	101.33	0.0036
0.0650	101.33	0.0065
0.1243	101.33	0.0100
0.2143	101.33	0.0159
0.3159	101.33	0.0223
0.4515	101.33	0.0318
0.5821	101.33	0.0449
0.6703	101.33	0.0599
0.7528	101.33	0.0805
0.8230	101.33	0.1141
0.8665	101.33	0.1527
0.8922	101.33	0.1883
0.9306	101.33	0.2714
0.9650	101.33	0.4508
0.9872	101.33	0.7062
0.9943	101.33	0.8495

Mole fraction of Eucalyptol (2) [ref]

Fixed		Measured
Mole fraction of Eucalyptol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Eucalyptol (2) - Gas
0.0047	33.33	0.0006
0.0500	33.33	0.0056
0.0719	33.33	0.0071
0.1193	33.33	0.0096
0.1816	33.33	0.0126
0.2161	33.33	0.0142
0.2901	33.33	0.0178
0.3814	33.33	0.0225
0.4586	33.33	0.0290
0.5952	33.33	0.0407
0.7105	33.33	0.0545
0.8154	33.33	0.0886
0.8429	33.33	0.1006
0.8940	33.33	0.1418
0.9190	33.33	0.1753
0.9460	33.33	0.2493
0.9773	33.33	0.4595
0.9856	33.33	0.5862
0.9959	33.33	0.8396
0.0097	66.66	0.0010
0.0266	66.66	0.0025
0.1011	66.66	0.0088
0.1736	66.66	0.0137
0.2898	66.66	0.0201
0.3823	66.66	0.0263
0.5073	66.66	0.0367
0.5933	66.66	0.0478
0.6947	66.66	0.0640
0.7858	66.66	0.0850
0.8244	66.66	0.0968
0.9043	66.66	0.1566
0.9320	66.66	0.2045
0.9659	66.66	0.3543
0.9805	66.66	0.4862
0.9939	66.66	0.7675
0.9979	66.66	0.9049
0.0154	101.33	0.0017
0.0337	101.33	0.0036
0.0650	101.33	0.0065
0.1243	101.33	0.0100
0.2143	101.33	0.0159
0.3159	101.33	0.0223
0.4515	101.33	0.0318
0.5821	101.33	0.0449
0.6703	101.33	0.0599
0.7528	101.33	0.0805
0.8230	101.33	0.1141
0.8665	101.33	0.1527
0.8922	101.33	0.1883
0.9306	101.33	0.2714
0.9650	101.33	0.4508
0.9872	101.33	0.7062
0.9943	101.33	0.8495

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
304.70	0.0000	115.30
304.70	0.0506	123.90
304.70	0.0990	132.00
304.70	0.1999	149.00
304.70	0.3007	166.00
304.70	0.3956	181.70
304.70	0.5002	199.40
304.70	0.5975	214.30
304.70	0.7017	231.60
304.70	0.8065	247.20
304.70	0.8964	259.80
304.70	0.9501	267.00
304.70	1.0000	273.30
309.60	0.0000	117.30
309.60	0.0506	126.20
309.60	0.0990	134.60
309.60	0.1999	151.80
309.60	0.3007	169.00
309.60	0.3956	184.90
309.60	0.5002	202.50
309.60	0.5975	217.40
309.60	0.7017	235.10
309.60	0.8065	250.50
309.60	0.8964	263.70
309.60	0.9501	269.90
309.60	1.0000	276.40
314.60	0.0000	119.60
314.60	0.0506	128.60
314.60	0.0990	137.10
314.60	0.1999	154.60
314.60	0.3007	171.80
314.60	0.3956	188.10
314.60	0.5002	205.50
314.60	0.5975	221.50
314.60	0.7017	238.00
314.60	0.8065	253.60
314.60	0.8964	267.00
314.60	0.9501	273.40
314.60	1.0000	279.50
319.50	0.0000	121.90
319.50	0.0506	131.10
319.50	0.0990	139.70
319.50	0.1999	157.10
319.50	0.3007	174.90
319.50	0.3956	191.10
319.50	0.5002	208.50
319.50	0.5975	224.50
319.50	0.7017	241.20
319.50	0.8065	256.70
319.50	0.8964	269.90
319.50	0.9501	275.80
319.50	1.0000	282.60
324.50	0.0000	124.20
324.50	0.0506	133.50
324.50	0.0990	142.10
324.50	0.1999	160.00
324.50	0.3007	177.70
324.50	0.3956	194.10
324.50	0.5002	211.30
324.50	0.5975	227.40
324.50	0.7017	244.10
324.50	0.8065	259.30
324.50	0.8964	272.50
324.50	0.9501	279.00
324.50	1.0000	285.10

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
304.70	0.0000	115.30
304.70	0.0506	123.90
304.70	0.0990	132.00
304.70	0.1999	149.00
304.70	0.3007	166.00
304.70	0.3956	181.70
304.70	0.5002	199.40
304.70	0.5975	214.30
304.70	0.7017	231.60
304.70	0.8065	247.20
304.70	0.8964	259.80
304.70	0.9501	267.00
304.70	1.0000	273.30
309.60	0.0000	117.30
309.60	0.0506	126.20
309.60	0.0990	134.60
309.60	0.1999	151.80
309.60	0.3007	169.00
309.60	0.3956	184.90
309.60	0.5002	202.50
309.60	0.5975	217.40
309.60	0.7017	235.10
309.60	0.8065	250.50
309.60	0.8964	263.70
309.60	0.9501	269.90
309.60	1.0000	276.40
314.60	0.0000	119.60
314.60	0.0506	128.60
314.60	0.0990	137.10
314.60	0.1999	154.60
314.60	0.3007	171.80
314.60	0.3956	188.10
314.60	0.5002	205.50
314.60	0.5975	221.50
314.60	0.7017	238.00
314.60	0.8065	253.60
314.60	0.8964	267.00
314.60	0.9501	273.40
314.60	1.0000	279.50
319.50	0.0000	121.90
319.50	0.0506	131.10
319.50	0.0990	139.70
319.50	0.1999	157.10
319.50	0.3007	174.90
319.50	0.3956	191.10
319.50	0.5002	208.50
319.50	0.5975	224.50
319.50	0.7017	241.20
319.50	0.8065	256.70
319.50	0.8964	269.90
319.50	0.9501	275.80
319.50	1.0000	282.60
324.50	0.0000	124.20
324.50	0.0506	133.50
324.50	0.0990	142.10
324.50	0.1999	160.00
324.50	0.3007	177.70
324.50	0.3956	194.10
324.50	0.5002	211.30
324.50	0.5975	227.40
324.50	0.7017	244.10
324.50	0.8065	259.30
324.50	0.8964	272.50
324.50	0.9501	279.00
324.50	1.0000	285.10

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	0.0852	2.10
278.15	0.1107	2.06
278.15	0.2121	1.94
278.15	0.2956	1.85
278.15	0.3929	1.74
278.15	0.5223	1.57
278.15	0.6648	1.36
278.15	0.7894	1.06
278.15	0.8307	0.94
278.15	0.9135	0.59
278.15	0.9764	0.25
283.15	0.0853	2.94
283.15	0.1108	2.89
283.15	0.2122	2.68
283.15	0.2958	2.56
283.15	0.3930	2.41
283.15	0.5224	2.17
283.15	0.6650	1.88
283.15	0.7895	1.46
283.15	0.8308	1.30
283.15	0.9136	0.81
283.15	0.9765	0.34
288.15	0.0854	4.03
288.15	0.1109	3.96
288.15	0.2124	3.68
288.15	0.2960	3.53
288.15	0.3932	3.30
288.15	0.5226	3.01
288.15	0.6652	2.56
288.15	0.7897	2.00
288.15	0.8309	1.77
288.15	0.9137	1.13
288.15	0.9765	0.44
293.15	0.0856	5.48
293.15	0.1111	5.38
293.15	0.2126	5.02
293.15	0.2963	4.75
293.15	0.3934	4.49
293.15	0.5229	4.08
293.15	0.6655	3.48
293.15	0.7899	2.72
293.15	0.8311	2.39
293.15	0.9138	1.52
293.15	0.9765	0.61
298.15	0.0859	7.31
298.15	0.1114	7.16
298.15	0.2128	6.67
298.15	0.2967	6.32
298.15	0.3936	5.92
298.15	0.5232	5.38
298.15	0.6659	4.61
298.15	0.7901	3.60
298.15	0.8313	3.18
298.15	0.9139	2.02
298.15	0.9766	0.81
303.15	0.0863	9.73
303.15	0.1118	9.55
303.15	0.2132	8.91
303.15	0.2973	8.43
303.15	0.3941	7.91
303.15	0.5237	7.18
303.15	0.6666	6.12
303.15	0.7904	4.82
303.15	0.8316	4.19
303.15	0.9141	2.65
303.15	0.9766	1.07
308.15	0.0869	12.80
308.15	0.1124	12.25
308.15	0.2139	11.72
308.15	0.2982	11.10
308.15	0.3946	10.43
308.15	0.5244	9.48
308.15	0.6675	8.09
308.15	0.7909	6.27
308.15	0.8320	5.51
308.15	0.9144	3.45
308.15	0.9767	1.40
313.15	0.0878	16.69
313.15	0.1132	16.39
313.15	0.2148	15.30
313.15	0.2995	14.48
313.15	0.3955	13.62
313.15	0.5255	12.35
313.15	0.6687	10.50
313.15	0.7916	8.14
313.15	0.8326	7.10
313.15	0.9147	4.48
313.15	0.9768	1.81
318.15	0.0891	21.51
318.15	0.1145	21.13
318.15	0.2161	19.72
318.15	0.3014	18.69
318.15	0.3968	17.58
318.15	0.5270	15.91
318.15	0.6705	13.46
318.15	0.7926	10.42
318.15	0.8334	9.05
318.15	0.9152	5.70
318.15	0.9769	2.32
323.15	0.0911	27.45
323.15	0.1164	26.96
323.15	0.2181	25.19
323.15	0.3042	23.83
323.15	0.3986	22.42
323.15	0.5291	20.24
323.15	0.6729	17.05
323.15	0.7938	13.15
323.15	0.8346	11.46
323.15	0.9157	7.21
323.15	0.9770	2.98

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	0.0852	2.10
278.15	0.1107	2.06
278.15	0.2121	1.94
278.15	0.2956	1.85
278.15	0.3929	1.74
278.15	0.5223	1.57
278.15	0.6648	1.36
278.15	0.7894	1.06
278.15	0.8307	0.94
278.15	0.9135	0.59
278.15	0.9764	0.25
283.15	0.0853	2.94
283.15	0.1108	2.89
283.15	0.2122	2.68
283.15	0.2958	2.56
283.15	0.3930	2.41
283.15	0.5224	2.17
283.15	0.6650	1.88
283.15	0.7895	1.46
283.15	0.8308	1.30
283.15	0.9136	0.81
283.15	0.9765	0.34
288.15	0.0854	4.03
288.15	0.1109	3.96
288.15	0.2124	3.68
288.15	0.2960	3.53
288.15	0.3932	3.30
288.15	0.5226	3.01
288.15	0.6652	2.56
288.15	0.7897	2.00
288.15	0.8309	1.77
288.15	0.9137	1.13
288.15	0.9765	0.44
293.15	0.0856	5.48
293.15	0.1111	5.38
293.15	0.2126	5.02
293.15	0.2963	4.75
293.15	0.3934	4.49
293.15	0.5229	4.08
293.15	0.6655	3.48
293.15	0.7899	2.72
293.15	0.8311	2.39
293.15	0.9138	1.52
293.15	0.9765	0.61
298.15	0.0859	7.31
298.15	0.1114	7.16
298.15	0.2128	6.67
298.15	0.2967	6.32
298.15	0.3936	5.92
298.15	0.5232	5.38
298.15	0.6659	4.61
298.15	0.7901	3.60
298.15	0.8313	3.18
298.15	0.9139	2.02
298.15	0.9766	0.81
303.15	0.0863	9.73
303.15	0.1118	9.55
303.15	0.2132	8.91
303.15	0.2973	8.43
303.15	0.3941	7.91
303.15	0.5237	7.18
303.15	0.6666	6.12
303.15	0.7904	4.82
303.15	0.8316	4.19
303.15	0.9141	2.65
303.15	0.9766	1.07
308.15	0.0869	12.80
308.15	0.1124	12.25
308.15	0.2139	11.72
308.15	0.2982	11.10
308.15	0.3946	10.43
308.15	0.5244	9.48
308.15	0.6675	8.09
308.15	0.7909	6.27
308.15	0.8320	5.51
308.15	0.9144	3.45
308.15	0.9767	1.40
313.15	0.0878	16.69
313.15	0.1132	16.39
313.15	0.2148	15.30
313.15	0.2995	14.48
313.15	0.3955	13.62
313.15	0.5255	12.35
313.15	0.6687	10.50
313.15	0.7916	8.14
313.15	0.8326	7.10
313.15	0.9147	4.48
313.15	0.9768	1.81
318.15	0.0891	21.51
318.15	0.1145	21.13
318.15	0.2161	19.72
318.15	0.3014	18.69
318.15	0.3968	17.58
318.15	0.5270	15.91
318.15	0.6705	13.46
318.15	0.7926	10.42
318.15	0.8334	9.05
318.15	0.9152	5.70
318.15	0.9769	2.32
323.15	0.0911	27.45
323.15	0.1164	26.96
323.15	0.2181	25.19
323.15	0.3042	23.83
323.15	0.3986	22.42
323.15	0.5291	20.24
323.15	0.6729	17.05
323.15	0.7938	13.15
323.15	0.8346	11.46
323.15	0.9157	7.21
323.15	0.9770	2.98

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	1.3594
298.15	0.0496	1.3724
298.15	0.1018	1.3837
298.15	0.2075	1.4018
298.15	0.2958	1.4132
298.15	0.4073	1.4246
298.15	0.5020	1.4322
298.15	0.6008	1.4388
298.15	0.6969	1.4439
298.15	0.8036	1.4487
298.15	0.8992	1.4522
298.15	0.9611	1.4542
298.15	1.0000	1.4553
313.15	0.0000	1.3532
313.15	0.0496	1.3662
313.15	0.1018	1.3774
313.15	0.2075	1.3953
313.15	0.2958	1.4067
313.15	0.4073	1.418
313.15	0.5020	1.4255
313.15	0.6008	1.432
313.15	0.6969	1.4371
313.15	0.8036	1.4418
313.15	0.8992	1.4453
313.15	0.9611	1.4472
313.15	1.0000	1.4483

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	1.3594
298.15	0.0496	1.3724
298.15	0.1018	1.3837
298.15	0.2075	1.4018
298.15	0.2958	1.4132
298.15	0.4073	1.4246
298.15	0.5020	1.4322
298.15	0.6008	1.4388
298.15	0.6969	1.4439
298.15	0.8036	1.4487
298.15	0.8992	1.4522
298.15	0.9611	1.4542
298.15	1.0000	1.4553
313.15	0.0000	1.3532
313.15	0.0496	1.3662
313.15	0.1018	1.3774
313.15	0.2075	1.3953
313.15	0.2958	1.4067
313.15	0.4073	1.418
313.15	0.5020	1.4255
313.15	0.6008	1.432
313.15	0.6969	1.4371
313.15	0.8036	1.4418
313.15	0.8992	1.4453
313.15	0.9611	1.4472
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	785.61
298.15	0.0496	804.82
298.15	0.1018	821.68
298.15	0.2075	847.95
298.15	0.2958	864.33
298.15	0.4073	880.16
298.15	0.5020	890.64
298.15	0.6008	899.4
298.15	0.6969	906.27
298.15	0.8036	912.42
298.15	0.8992	916.75
298.15	0.9611	919.09
298.15	1.0000	920.24
313.15	0.0000	772.55
313.15	0.0496	791.71
313.15	0.1018	808.55
313.15	0.2075	834.78
313.15	0.2958	851.16
313.15	0.4073	867.0
313.15	0.5020	877.48
313.15	0.6008	886.26
313.15	0.6969	893.15
313.15	0.8036	899.33
313.15	0.8992	903.71
313.15	0.9611	906.1
313.15	1.0000	907.29

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	0.0000	797.9
283.15	100.00	0.0983	833.3
283.15	100.00	0.1991	858.9
283.15	100.00	0.2954	877.2
283.15	100.00	0.3901	891.1
283.15	100.00	0.4930	902.9
283.15	100.00	0.5980	912.3
283.15	100.00	0.6981	919.3
283.15	100.00	0.7967	924.9
283.15	100.00	0.8898	929.2
283.15	100.00	1.0000	933.3
283.15	5000.00	0.0000	802.0
283.15	5000.00	0.0983	837.2
283.15	5000.00	0.1991	862.6
283.15	5000.00	0.2954	880.8
283.15	5000.00	0.3901	894.6
283.15	5000.00	0.4930	906.4
283.15	5000.00	0.5980	915.8
283.15	5000.00	0.6981	922.8
283.15	5000.00	0.7967	928.3
283.15	5000.00	0.8898	932.7
283.15	5000.00	1.0000	936.7
283.15	10000.00	0.0000	805.9
283.15	10000.00	0.0983	841.0
283.15	10000.00	0.1991	866.2
283.15	10000.00	0.2954	884.2
283.15	10000.00	0.3901	898.0
283.15	10000.00	0.4930	909.7
283.15	10000.00	0.5980	919.1
283.15	10000.00	0.6981	926.0
283.15	10000.00	0.7967	931.5
283.15	10000.00	0.8898	935.9
283.15	10000.00	1.0000	939.9
283.15	15000.00	0.0000	809.7
283.15	15000.00	0.0983	844.5
283.15	15000.00	0.1991	869.7
283.15	15000.00	0.2954	887.7
283.15	15000.00	0.3901	901.4
283.15	15000.00	0.4930	913.0
283.15	15000.00	0.5980	922.3
283.15	15000.00	0.6981	929.3
283.15	15000.00	0.7967	934.7
283.15	15000.00	0.8898	939.0
283.15	15000.00	1.0000	943.1
283.15	20000.00	0.0000	813.4
283.15	20000.00	0.0983	848.0
283.15	20000.00	0.1991	873.0
283.15	20000.00	0.2954	891.0
283.15	20000.00	0.3901	904.7
283.15	20000.00	0.4930	916.2
283.15	20000.00	0.5980	925.5
283.15	20000.00	0.6981	932.4
283.15	20000.00	0.7967	937.8
283.15	20000.00	0.8898	942.1
283.15	20000.00	1.0000	946.2
298.15	100.00	0.0000	784.9
298.15	100.00	0.0983	819.9
298.15	100.00	0.1991	845.7
298.15	100.00	0.2954	864.3
298.15	100.00	0.3901	878.2
298.15	100.00	0.4930	889.9
298.15	100.00	0.5980	899.3
298.15	100.00	0.6981	906.4
298.15	100.00	0.7967	912.1
298.15	100.00	0.8898	916.4
298.15	100.00	1.0000	920.4
298.15	5000.00	0.0000	789.3
298.15	5000.00	0.0983	823.9
298.15	5000.00	0.1991	849.7
298.15	5000.00	0.2954	868.1
298.15	5000.00	0.3901	882.0
298.15	5000.00	0.4930	893.7
298.15	5000.00	0.5980	903.1
298.15	5000.00	0.6981	910.2
298.15	5000.00	0.7967	915.8
298.15	5000.00	0.8898	920.1
298.15	5000.00	1.0000	924.1
298.15	10000.00	0.0000	793.7
298.15	10000.00	0.0983	828.1
298.15	10000.00	0.1991	853.7
298.15	10000.00	0.2954	872.0
298.15	10000.00	0.3901	885.7
298.15	10000.00	0.4930	897.4
298.15	10000.00	0.5980	906.7
298.15	10000.00	0.6981	913.8
298.15	10000.00	0.7967	919.3
298.15	10000.00	0.8898	923.6
298.15	10000.00	1.0000	927.7
298.15	15000.00	0.0000	797.8
298.15	15000.00	0.0983	832.0
298.15	15000.00	0.1991	857.5
298.15	15000.00	0.2954	875.7
298.15	15000.00	0.3901	889.4
298.15	15000.00	0.4930	901.1
298.15	15000.00	0.5980	910.3
298.15	15000.00	0.6981	917.3
298.15	15000.00	0.7967	922.7
298.15	15000.00	0.8898	927.1
298.15	15000.00	1.0000	931.2
298.15	20000.00	0.0000	801.5
298.15	20000.00	0.0983	835.5
298.15	20000.00	0.1991	861.0
298.15	20000.00	0.2954	879.1
298.15	20000.00	0.3901	892.7
298.15	20000.00	0.4930	904.3
298.15	20000.00	0.5980	913.5
298.15	20000.00	0.6981	920.4
298.15	20000.00	0.7967	925.9
298.15	20000.00	0.8898	930.2
298.15	20000.00	1.0000	934.4
313.15	100.00	0.0000	772.0
313.15	100.00	0.0983	807.2
313.15	100.00	0.1991	832.7
313.15	100.00	0.2954	851.2
313.15	100.00	0.3901	865.0
313.15	100.00	0.4930	876.8
313.15	100.00	0.5980	886.2
313.15	100.00	0.6981	893.3
313.15	100.00	0.7967	898.8
313.15	100.00	0.8898	903.2
313.15	100.00	1.0000	907.3
313.15	5000.00	0.0000	777.0
313.15	5000.00	0.0983	812.0
313.15	5000.00	0.1991	837.3
313.15	5000.00	0.2954	855.6
313.15	5000.00	0.3901	869.4
313.15	5000.00	0.4930	881.0
313.15	5000.00	0.5980	890.4
313.15	5000.00	0.6981	897.5
313.15	5000.00	0.7967	902.9
313.15	5000.00	0.8898	907.3
313.15	5000.00	1.0000	911.4
313.15	10000.00	0.0000	781.5
313.15	10000.00	0.0983	816.3
313.15	10000.00	0.1991	841.5
313.15	10000.00	0.2954	859.7
313.15	10000.00	0.3901	873.4
313.15	10000.00	0.4930	884.9
313.15	10000.00	0.5980	894.2
313.15	10000.00	0.6981	901.3
313.15	10000.00	0.7967	906.7
313.15	10000.00	0.8898	911.0
313.15	10000.00	1.0000	915.2
313.15	15000.00	0.0000	786.0
313.15	15000.00	0.0983	820.7
313.15	15000.00	0.1991	845.7
313.15	15000.00	0.2954	863.8
313.15	15000.00	0.3901	877.4
313.15	15000.00	0.4930	888.9
313.15	15000.00	0.5980	898.1
313.15	15000.00	0.6981	905.1
313.15	15000.00	0.7967	910.6
313.15	15000.00	0.8898	914.8
313.15	15000.00	1.0000	919.0
313.15	20000.00	0.0000	790.1
313.15	20000.00	0.0983	824.7
313.15	20000.00	0.1991	849.5
313.15	20000.00	0.2954	867.5
313.15	20000.00	0.3901	881.1
313.15	20000.00	0.4930	892.5
313.15	20000.00	0.5980	901.7
313.15	20000.00	0.6981	908.6
313.15	20000.00	0.7967	914.1
313.15	20000.00	0.8898	918.3
313.15	20000.00	1.0000	922.5

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	785.61
298.15	0.0496	804.82
298.15	0.1018	821.68
298.15	0.2075	847.95
298.15	0.2958	864.33
298.15	0.4073	880.16
298.15	0.5020	890.64
298.15	0.6008	899.4
298.15	0.6969	906.27
298.15	0.8036	912.42
298.15	0.8992	916.75
298.15	0.9611	919.09
298.15	1.0000	920.24
313.15	0.0000	772.55
313.15	0.0496	791.71
313.15	0.1018	808.55
313.15	0.2075	834.78
313.15	0.2958	851.16
313.15	0.4073	867.0
313.15	0.5020	877.48
313.15	0.6008	886.26
313.15	0.6969	893.15
313.15	0.8036	899.33
313.15	0.8992	903.71
313.15	0.9611	906.1
313.15	1.0000	907.29

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Eucalyptol (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	0.0000	797.9
283.15	100.00	0.0983	833.3
283.15	100.00	0.1991	858.9
283.15	100.00	0.2954	877.2
283.15	100.00	0.3901	891.1
283.15	100.00	0.4930	902.9
283.15	100.00	0.5980	912.3
283.15	100.00	0.6981	919.3
283.15	100.00	0.7967	924.9
283.15	100.00	0.8898	929.2
283.15	100.00	1.0000	933.3
283.15	5000.00	0.0000	802.0
283.15	5000.00	0.0983	837.2
283.15	5000.00	0.1991	862.6
283.15	5000.00	0.2954	880.8
283.15	5000.00	0.3901	894.6
283.15	5000.00	0.4930	906.4
283.15	5000.00	0.5980	915.8
283.15	5000.00	0.6981	922.8
283.15	5000.00	0.7967	928.3
283.15	5000.00	0.8898	932.7
283.15	5000.00	1.0000	936.7
283.15	10000.00	0.0000	805.9
283.15	10000.00	0.0983	841.0
283.15	10000.00	0.1991	866.2
283.15	10000.00	0.2954	884.2
283.15	10000.00	0.3901	898.0
283.15	10000.00	0.4930	909.7
283.15	10000.00	0.5980	919.1
283.15	10000.00	0.6981	926.0
283.15	10000.00	0.7967	931.5
283.15	10000.00	0.8898	935.9
283.15	10000.00	1.0000	939.9
283.15	15000.00	0.0000	809.7
283.15	15000.00	0.0983	844.5
283.15	15000.00	0.1991	869.7
283.15	15000.00	0.2954	887.7
283.15	15000.00	0.3901	901.4
283.15	15000.00	0.4930	913.0
283.15	15000.00	0.5980	922.3
283.15	15000.00	0.6981	929.3
283.15	15000.00	0.7967	934.7
283.15	15000.00	0.8898	939.0
283.15	15000.00	1.0000	943.1
283.15	20000.00	0.0000	813.4
283.15	20000.00	0.0983	848.0
283.15	20000.00	0.1991	873.0
283.15	20000.00	0.2954	891.0
283.15	20000.00	0.3901	904.7
283.15	20000.00	0.4930	916.2
283.15	20000.00	0.5980	925.5
283.15	20000.00	0.6981	932.4
283.15	20000.00	0.7967	937.8
283.15	20000.00	0.8898	942.1
283.15	20000.00	1.0000	946.2
298.15	100.00	0.0000	784.9
298.15	100.00	0.0983	819.9
298.15	100.00	0.1991	845.7
298.15	100.00	0.2954	864.3
298.15	100.00	0.3901	878.2
298.15	100.00	0.4930	889.9
298.15	100.00	0.5980	899.3
298.15	100.00	0.6981	906.4
298.15	100.00	0.7967	912.1
298.15	100.00	0.8898	916.4
298.15	100.00	1.0000	920.4
298.15	5000.00	0.0000	789.3
298.15	5000.00	0.0983	823.9
298.15	5000.00	0.1991	849.7
298.15	5000.00	0.2954	868.1
298.15	5000.00	0.3901	882.0
298.15	5000.00	0.4930	893.7
298.15	5000.00	0.5980	903.1
298.15	5000.00	0.6981	910.2
298.15	5000.00	0.7967	915.8
298.15	5000.00	0.8898	920.1
298.15	5000.00	1.0000	924.1
298.15	10000.00	0.0000	793.7
298.15	10000.00	0.0983	828.1
298.15	10000.00	0.1991	853.7
298.15	10000.00	0.2954	872.0
298.15	10000.00	0.3901	885.7
298.15	10000.00	0.4930	897.4
298.15	10000.00	0.5980	906.7
298.15	10000.00	0.6981	913.8
298.15	10000.00	0.7967	919.3
298.15	10000.00	0.8898	923.6
298.15	10000.00	1.0000	927.7
298.15	15000.00	0.0000	797.8
298.15	15000.00	0.0983	832.0
298.15	15000.00	0.1991	857.5
298.15	15000.00	0.2954	875.7
298.15	15000.00	0.3901	889.4
298.15	15000.00	0.4930	901.1
298.15	15000.00	0.5980	910.3
298.15	15000.00	0.6981	917.3
298.15	15000.00	0.7967	922.7
298.15	15000.00	0.8898	927.1
298.15	15000.00	1.0000	931.2
298.15	20000.00	0.0000	801.5
298.15	20000.00	0.0983	835.5
298.15	20000.00	0.1991	861.0
298.15	20000.00	0.2954	879.1
298.15	20000.00	0.3901	892.7
298.15	20000.00	0.4930	904.3
298.15	20000.00	0.5980	913.5
298.15	20000.00	0.6981	920.4
298.15	20000.00	0.7967	925.9
298.15	20000.00	0.8898	930.2
298.15	20000.00	1.0000	934.4
313.15	100.00	0.0000	772.0
313.15	100.00	0.0983	807.2
313.15	100.00	0.1991	832.7
313.15	100.00	0.2954	851.2
313.15	100.00	0.3901	865.0
313.15	100.00	0.4930	876.8
313.15	100.00	0.5980	886.2
313.15	100.00	0.6981	893.3
313.15	100.00	0.7967	898.8
313.15	100.00	0.8898	903.2
313.15	100.00	1.0000	907.3
313.15	5000.00	0.0000	777.0
313.15	5000.00	0.0983	812.0
313.15	5000.00	0.1991	837.3
313.15	5000.00	0.2954	855.6
313.15	5000.00	0.3901	869.4
313.15	5000.00	0.4930	881.0
313.15	5000.00	0.5980	890.4
313.15	5000.00	0.6981	897.5
313.15	5000.00	0.7967	902.9
313.15	5000.00	0.8898	907.3
313.15	5000.00	1.0000	911.4
313.15	10000.00	0.0000	781.5
313.15	10000.00	0.0983	816.3
313.15	10000.00	0.1991	841.5
313.15	10000.00	0.2954	859.7
313.15	10000.00	0.3901	873.4
313.15	10000.00	0.4930	884.9
313.15	10000.00	0.5980	894.2
313.15	10000.00	0.6981	901.3
313.15	10000.00	0.7967	906.7
313.15	10000.00	0.8898	911.0
313.15	10000.00	1.0000	915.2
313.15	15000.00	0.0000	786.0
313.15	15000.00	0.0983	820.7
313.15	15000.00	0.1991	845.7
313.15	15000.00	0.2954	863.8
313.15	15000.00	0.3901	877.4
313.15	15000.00	0.4930	888.9
313.15	15000.00	0.5980	898.1
313.15	15000.00	0.6981	905.1
313.15	15000.00	0.7967	910.6
313.15	15000.00	0.8898	914.8
313.15	15000.00	1.0000	919.0
313.15	20000.00	0.0000	790.1
313.15	20000.00	0.0983	824.7
313.15	20000.00	0.1991	849.5
313.15	20000.00	0.2954	867.5
313.15	20000.00	0.3901	881.1
313.15	20000.00	0.4930	892.5
313.15	20000.00	0.5980	901.7
313.15	20000.00	0.6981	908.6
313.15	20000.00	0.7967	914.1
313.15	20000.00	0.8898	918.3
313.15	20000.00	1.0000	922.5

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	1144.7
298.15	0.0496	1168.4
298.15	0.1018	1186.7
298.15	0.2075	1213.7
298.15	0.2958	1229.6
298.15	0.4073	1245.3
298.15	0.5020	1255.5
298.15	0.6008	1264.7
298.15	0.6969	1270.7
298.15	0.8036	1275.8
298.15	0.8992	1278.7
298.15	0.9611	1280.4
298.15	1.0000	1280.1
313.15	0.0000	1094.1
313.15	0.0496	1113.3
313.15	0.1018	1130.6
313.15	0.2075	1157.2
313.15	0.2958	1173.6
313.15	0.4073	1189.0
313.15	0.5020	1198.9
313.15	0.6008	1206.9
313.15	0.6969	1212.9
313.15	0.8036	1217.7
313.15	0.8992	1220.4
313.15	0.9611	1221.5
313.15	1.0000	1221.1

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	1144.7
298.15	0.0496	1168.4
298.15	0.1018	1186.7
298.15	0.2075	1213.7
298.15	0.2958	1229.6
298.15	0.4073	1245.3
298.15	0.5020	1255.5
298.15	0.6008	1264.7
298.15	0.6969	1270.7
298.15	0.8036	1275.8
298.15	0.8992	1278.7
298.15	0.9611	1280.4
298.15	1.0000	1280.1
313.15	0.0000	1094.1
313.15	0.0496	1113.3
313.15	0.1018	1130.6
313.15	0.2075	1157.2
313.15	0.2958	1173.6
313.15	0.4073	1189.0
313.15	0.5020	1198.9
313.15	0.6008	1206.9
313.15	0.6969	1212.9
313.15	0.8036	1217.7
313.15	0.8992	1220.4
313.15	0.9611	1221.5
313.15	1.0000	1221.1

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Eucalyptol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0047	33.33	326.10
0.0500	33.33	326.50
0.0719	33.33	326.40
0.1193	33.33	326.70
0.1816	33.33	327.70
0.2161	33.33	328.10
0.2901	33.33	329.10
0.3814	33.33	330.60
0.4586	33.33	332.10
0.5952	33.33	335.90
0.7105	33.33	340.30
0.8154	33.33	347.90
0.8429	33.33	350.10
0.8940	33.33	356.80
0.9190	33.33	361.30
0.9460	33.33	369.30
0.9773	33.33	385.00
0.9856	33.33	392.00
0.9959	33.33	403.10
0.0097	66.66	341.10
0.0266	66.66	341.20
0.1011	66.66	342.50
0.1736	66.66	343.70
0.2898	66.66	345.30
0.3823	66.66	347.00
0.5073	66.66	349.90
0.5933	66.66	352.70
0.6947	66.66	357.50
0.7858	66.66	362.80
0.8244	66.66	365.40
0.9043	66.66	376.10
0.9320	66.66	383.00
0.9659	66.66	397.90
0.9805	66.66	408.00
0.9939	66.66	422.50
0.9979	66.66	428.70
0.0154	101.33	351.50
0.0337	101.33	351.60
0.0650	101.33	351.90
0.1243	101.33	353.00
0.2143	101.33	354.60
0.3159	101.33	356.50
0.4515	101.33	359.70
0.5821	101.33	363.90
0.6703	101.33	368.40
0.7528	101.33	374.00
0.8230	101.33	381.50
0.8665	101.33	388.40
0.8922	101.33	393.80
0.9306	101.33	404.90
0.9650	101.33	420.40
0.9872	101.33	436.00
0.9943	101.33	442.70

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Eucalyptol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0047	33.33	326.10
0.0500	33.33	326.50
0.0719	33.33	326.40
0.1193	33.33	326.70
0.1816	33.33	327.70
0.2161	33.33	328.10
0.2901	33.33	329.10
0.3814	33.33	330.60
0.4586	33.33	332.10
0.5952	33.33	335.90
0.7105	33.33	340.30
0.8154	33.33	347.90
0.8429	33.33	350.10
0.8940	33.33	356.80
0.9190	33.33	361.30
0.9460	33.33	369.30
0.9773	33.33	385.00
0.9856	33.33	392.00
0.9959	33.33	403.10
0.0097	66.66	341.10
0.0266	66.66	341.20
0.1011	66.66	342.50
0.1736	66.66	343.70
0.2898	66.66	345.30
0.3823	66.66	347.00
0.5073	66.66	349.90
0.5933	66.66	352.70
0.6947	66.66	357.50
0.7858	66.66	362.80
0.8244	66.66	365.40
0.9043	66.66	376.10
0.9320	66.66	383.00
0.9659	66.66	397.90
0.9805	66.66	408.00
0.9939	66.66	422.50
0.9979	66.66	428.70
0.0154	101.33	351.50
0.0337	101.33	351.60
0.0650	101.33	351.90
0.1243	101.33	353.00
0.2143	101.33	354.60
0.3159	101.33	356.50
0.4515	101.33	359.70
0.5821	101.33	363.90
0.6703	101.33	368.40
0.7528	101.33	374.00
0.8230	101.33	381.50
0.8665	101.33	388.40
0.8922	101.33	393.80
0.9306	101.33	404.90
0.9650	101.33	420.40
0.9872	101.33	436.00
0.9943	101.33	442.70

Sources

• Total vapour pressure and excess Gibbs energy of ethanol with 1,8-cineole at temperatures between 278.15 K and 323.15 K
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Molar heat capacities of the mixture {1,8-cineole + ethanol} at several temperatures and atmospheric pressure
• Isobaric VLE of the mixture {1,8-cineole + ethanol}. EOS analysis and COSMO-RS modeling
• Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol