Mixture of Ethanol, 2-methoxy- + 1-Propanamine, N-propyl-

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	291.15	738.47
0.0000	293.15	737.2
0.0000	298.15	732.56
0.0000	303.15	728.2
0.0000	308.15	723.64
0.0501	291.15	746.83
0.0501	293.15	745.26
0.0501	298.15	740.37
0.0501	303.15	735.86
0.0501	308.15	731.07
0.1000	291.15	754.98
0.1000	293.15	753.42
0.1000	298.15	748.52
0.1000	303.15	743.91
0.1000	308.15	739.04
0.1502	291.15	763.4
0.1502	293.15	761.9
0.1502	298.15	756.9
0.1502	303.15	752.27
0.1502	308.15	747.36
0.2001	291.15	772.06
0.2001	293.15	770.51
0.2001	298.15	765.5
0.2001	303.15	760.85
0.2001	308.15	755.94
0.2508	291.15	781.14
0.2508	293.15	779.61
0.2508	298.15	774.59
0.2508	303.15	769.92
0.2508	308.15	764.98
0.2999	291.15	790.26
0.2999	293.15	788.66
0.2999	298.15	783.68
0.2999	303.15	778.97
0.2999	308.15	774.07
0.3502	291.15	799.92
0.3502	293.15	798.35
0.3502	298.15	793.28
0.3502	303.15	788.57
0.3502	308.15	783.65
0.4000	291.15	809.92
0.4000	293.15	808.21
0.4000	298.15	803.2
0.4000	303.15	798.45
0.4000	308.15	793.51
0.4500	291.15	820.34
0.4500	293.15	818.67
0.4500	298.15	813.61
0.4500	303.15	808.82
0.4500	308.15	803.85
0.4999	291.15	831.06
0.4999	293.15	829.4
0.4999	298.15	824.3
0.4999	303.15	819.53
0.4999	308.15	814.5
0.5507	291.15	842.47
0.5507	293.15	840.75
0.5507	298.15	835.6
0.5507	303.15	830.8
0.5507	308.15	825.78
0.5982	291.15	853.45
0.5982	293.15	851.69
0.5982	298.15	846.6
0.5982	303.15	841.77
0.5982	308.15	836.69
0.6502	291.15	866.02
0.6502	293.15	864.26
0.6502	298.15	859.11
0.6502	303.15	854.24
0.6502	308.15	849.17
0.6999	291.15	878.41
0.6999	293.15	876.59
0.6999	298.15	871.47
0.6999	303.15	866.58
0.6999	308.15	861.5
0.7489	291.15	891.21
0.7489	293.15	889.34
0.7489	298.15	884.21
0.7489	303.15	879.3
0.7489	308.15	874.18
0.8015	291.15	905.66
0.8015	293.15	903.7
0.8015	298.15	898.54
0.8015	303.15	893.64
0.8015	308.15	888.51
0.8496	291.15	919.22
0.8496	293.15	917.32
0.8496	298.15	912.15
0.8496	303.15	907.23
0.8496	308.15	902.13
0.8997	291.15	934.42
0.8997	293.15	932.35
0.8997	298.15	927.21
0.8997	303.15	922.3
0.8997	308.15	917.11
0.9497	291.15	950.19
0.9497	293.15	948.22
0.9497	298.15	943.1
0.9497	303.15	938.3
0.9497	308.15	933.24
1.0000	291.15	966.52
1.0000	293.15	964.88
1.0000	298.15	960.29
1.0000	303.15	955.76
1.0000	308.15	951.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	291.15	738.47
0.0000	293.15	737.2
0.0000	298.15	732.56
0.0000	303.15	728.2
0.0000	308.15	723.64
0.0501	291.15	746.83
0.0501	293.15	745.26
0.0501	298.15	740.37
0.0501	303.15	735.86
0.0501	308.15	731.07
0.1000	291.15	754.98
0.1000	293.15	753.42
0.1000	298.15	748.52
0.1000	303.15	743.91
0.1000	308.15	739.04
0.1502	291.15	763.4
0.1502	293.15	761.9
0.1502	298.15	756.9
0.1502	303.15	752.27
0.1502	308.15	747.36
0.2001	291.15	772.06
0.2001	293.15	770.51
0.2001	298.15	765.5
0.2001	303.15	760.85
0.2001	308.15	755.94
0.2508	291.15	781.14
0.2508	293.15	779.61
0.2508	298.15	774.59
0.2508	303.15	769.92
0.2508	308.15	764.98
0.2999	291.15	790.26
0.2999	293.15	788.66
0.2999	298.15	783.68
0.2999	303.15	778.97
0.2999	308.15	774.07
0.3502	291.15	799.92
0.3502	293.15	798.35
0.3502	298.15	793.28
0.3502	303.15	788.57
0.3502	308.15	783.65
0.4000	291.15	809.92
0.4000	293.15	808.21
0.4000	298.15	803.2
0.4000	303.15	798.45
0.4000	308.15	793.51
0.4500	291.15	820.34
0.4500	293.15	818.67
0.4500	298.15	813.61
0.4500	303.15	808.82
0.4500	308.15	803.85
0.4999	291.15	831.06
0.4999	293.15	829.4
0.4999	298.15	824.3
0.4999	303.15	819.53
0.4999	308.15	814.5
0.5507	291.15	842.47
0.5507	293.15	840.75
0.5507	298.15	835.6
0.5507	303.15	830.8
0.5507	308.15	825.78
0.5982	291.15	853.45
0.5982	293.15	851.69
0.5982	298.15	846.6
0.5982	303.15	841.77
0.5982	308.15	836.69
0.6502	291.15	866.02
0.6502	293.15	864.26
0.6502	298.15	859.11
0.6502	303.15	854.24
0.6502	308.15	849.17
0.6999	291.15	878.41
0.6999	293.15	876.59
0.6999	298.15	871.47
0.6999	303.15	866.58
0.6999	308.15	861.5
0.7489	291.15	891.21
0.7489	293.15	889.34
0.7489	298.15	884.21
0.7489	303.15	879.3
0.7489	308.15	874.18
0.8015	291.15	905.66
0.8015	293.15	903.7
0.8015	298.15	898.54
0.8015	303.15	893.64
0.8015	308.15	888.51
0.8496	291.15	919.22
0.8496	293.15	917.32
0.8496	298.15	912.15
0.8496	303.15	907.23
0.8496	308.15	902.13
0.8997	291.15	934.42
0.8997	293.15	932.35
0.8997	298.15	927.21
0.8997	303.15	922.3
0.8997	308.15	917.11
0.9497	291.15	950.19
0.9497	293.15	948.22
0.9497	298.15	943.1
0.9497	303.15	938.3
0.9497	308.15	933.24
1.0000	291.15	966.52
1.0000	293.15	964.88
1.0000	298.15	960.29
1.0000	303.15	955.76
1.0000	308.15	951.1

Sources

• Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures