Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0550 | 0.0006 |
| 298.15 | 0.1509 | 0.0007 |
| 298.15 | 0.2513 | 0.0008 |
| 298.15 | 0.3489 | 0.0009 |
| 298.15 | 0.4511 | 0.0011 |
| 298.15 | 0.5015 | 0.0012 |
| 298.15 | 0.5525 | 0.0013 |
| 298.15 | 0.6512 | 0.0015 |
| 298.15 | 0.7494 | 0.0018 |
| 298.15 | 0.8498 | 0.0021 |
| 298.15 | 0.9541 | 0.0026 |
| 308.15 | 0.0550 | 0.0005 |
| 308.15 | 0.1509 | 0.0006 |
| 308.15 | 0.2513 | 0.0007 |
| 308.15 | 0.3489 | 0.0008 |
| 308.15 | 0.4511 | 0.0009 |
| 308.15 | 0.5015 | 0.0010 |
| 308.15 | 0.5525 | 0.0010 |
| 308.15 | 0.6512 | 0.0012 |
| 308.15 | 0.7494 | 0.0014 |
| 308.15 | 0.8498 | 0.0017 |
| 308.15 | 0.9541 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0550 | 0.0006 |
| 298.15 | 0.1509 | 0.0007 |
| 298.15 | 0.2513 | 0.0008 |
| 298.15 | 0.3489 | 0.0009 |
| 298.15 | 0.4511 | 0.0011 |
| 298.15 | 0.5015 | 0.0012 |
| 298.15 | 0.5525 | 0.0013 |
| 298.15 | 0.6512 | 0.0015 |
| 298.15 | 0.7494 | 0.0018 |
| 298.15 | 0.8498 | 0.0021 |
| 298.15 | 0.9541 | 0.0026 |
| 308.15 | 0.0550 | 0.0005 |
| 308.15 | 0.1509 | 0.0006 |
| 308.15 | 0.2513 | 0.0007 |
| 308.15 | 0.3489 | 0.0008 |
| 308.15 | 0.4511 | 0.0009 |
| 308.15 | 0.5015 | 0.0010 |
| 308.15 | 0.5525 | 0.0010 |
| 308.15 | 0.6512 | 0.0012 |
| 308.15 | 0.7494 | 0.0014 |
| 308.15 | 0.8498 | 0.0017 |
| 308.15 | 0.9541 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0550 | 863.84 |
| 298.15 | 0.1509 | 867.24 |
| 298.15 | 0.2513 | 871.21 |
| 298.15 | 0.3489 | 875.19 |
| 298.15 | 0.4511 | 879.27 |
| 298.15 | 0.5015 | 881.19 |
| 298.15 | 0.5525 | 883.06 |
| 298.15 | 0.6512 | 886.44 |
| 298.15 | 0.7494 | 889.48 |
| 298.15 | 0.8498 | 892.31 |
| 298.15 | 0.9541 | 895.06 |
| 303.15 | 0.0550 | 859.17 |
| 303.15 | 0.1509 | 862.55 |
| 303.15 | 0.2513 | 866.52 |
| 303.15 | 0.3489 | 870.52 |
| 303.15 | 0.4511 | 874.63 |
| 303.15 | 0.5015 | 876.58 |
| 303.15 | 0.5525 | 878.48 |
| 303.15 | 0.6512 | 881.93 |
| 303.15 | 0.7494 | 885.06 |
| 303.15 | 0.8498 | 887.97 |
| 303.15 | 0.9541 | 890.8 |
| 308.15 | 0.0550 | 854.65 |
| 308.15 | 0.1509 | 858.08 |
| 308.15 | 0.2513 | 861.96 |
| 308.15 | 0.3489 | 865.88 |
| 308.15 | 0.4511 | 870.03 |
| 308.15 | 0.5015 | 872.06 |
| 308.15 | 0.5525 | 874.08 |
| 308.15 | 0.6512 | 877.86 |
| 308.15 | 0.7494 | 881.39 |
| 308.15 | 0.8498 | 884.68 |
| 308.15 | 0.9541 | 887.71 |
| 313.15 | 0.0550 | 849.76 |
| 313.15 | 0.1509 | 852.99 |
| 313.15 | 0.2513 | 856.75 |
| 313.15 | 0.3489 | 860.6 |
| 313.15 | 0.4511 | 864.68 |
| 313.15 | 0.5015 | 866.66 |
| 313.15 | 0.5525 | 868.64 |
| 313.15 | 0.6512 | 872.33 |
| 313.15 | 0.7494 | 875.78 |
| 313.15 | 0.8498 | 879.04 |
| 313.15 | 0.9541 | 882.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0550 | 863.84 |
| 298.15 | 0.1509 | 867.24 |
| 298.15 | 0.2513 | 871.21 |
| 298.15 | 0.3489 | 875.19 |
| 298.15 | 0.4511 | 879.27 |
| 298.15 | 0.5015 | 881.19 |
| 298.15 | 0.5525 | 883.06 |
| 298.15 | 0.6512 | 886.44 |
| 298.15 | 0.7494 | 889.48 |
| 298.15 | 0.8498 | 892.31 |
| 298.15 | 0.9541 | 895.06 |
| 303.15 | 0.0550 | 859.17 |
| 303.15 | 0.1509 | 862.55 |
| 303.15 | 0.2513 | 866.52 |
| 303.15 | 0.3489 | 870.52 |
| 303.15 | 0.4511 | 874.63 |
| 303.15 | 0.5015 | 876.58 |
| 303.15 | 0.5525 | 878.48 |
| 303.15 | 0.6512 | 881.93 |
| 303.15 | 0.7494 | 885.06 |
| 303.15 | 0.8498 | 887.97 |
| 303.15 | 0.9541 | 890.8 |
| 308.15 | 0.0550 | 854.65 |
| 308.15 | 0.1509 | 858.08 |
| 308.15 | 0.2513 | 861.96 |
| 308.15 | 0.3489 | 865.88 |
| 308.15 | 0.4511 | 870.03 |
| 308.15 | 0.5015 | 872.06 |
| 308.15 | 0.5525 | 874.08 |
| 308.15 | 0.6512 | 877.86 |
| 308.15 | 0.7494 | 881.39 |
| 308.15 | 0.8498 | 884.68 |
| 308.15 | 0.9541 | 887.71 |
| 313.15 | 0.0550 | 849.76 |
| 313.15 | 0.1509 | 852.99 |
| 313.15 | 0.2513 | 856.75 |
| 313.15 | 0.3489 | 860.6 |
| 313.15 | 0.4511 | 864.68 |
| 313.15 | 0.5015 | 866.66 |
| 313.15 | 0.5525 | 868.64 |
| 313.15 | 0.6512 | 872.33 |
| 313.15 | 0.7494 | 875.78 |
| 313.15 | 0.8498 | 879.04 |
| 313.15 | 0.9541 | 882.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0550 | 1303.0 |
| 298.15 | 0.1509 | 1301.0 |
| 298.15 | 0.2513 | 1302.0 |
| 298.15 | 0.3489 | 1303.0 |
| 298.15 | 0.4511 | 1304.0 |
| 298.15 | 0.5015 | 1305.0 |
| 298.15 | 0.5525 | 1306.0 |
| 298.15 | 0.6512 | 1306.0 |
| 298.15 | 0.7494 | 1306.0 |
| 298.15 | 0.8498 | 1306.0 |
| 298.15 | 0.9541 | 1305.0 |
| 308.15 | 0.0550 | 1261.0 |
| 308.15 | 0.1509 | 1260.0 |
| 308.15 | 0.2513 | 1261.0 |
| 308.15 | 0.3489 | 1262.0 |
| 308.15 | 0.4511 | 1264.0 |
| 308.15 | 0.5015 | 1265.0 |
| 308.15 | 0.5525 | 1267.0 |
| 308.15 | 0.6512 | 1270.0 |
| 308.15 | 0.7494 | 1273.0 |
| 308.15 | 0.8498 | 1277.0 |
| 308.15 | 0.9541 | 1282.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0550 | 1303.0 |
| 298.15 | 0.1509 | 1301.0 |
| 298.15 | 0.2513 | 1302.0 |
| 298.15 | 0.3489 | 1303.0 |
| 298.15 | 0.4511 | 1304.0 |
| 298.15 | 0.5015 | 1305.0 |
| 298.15 | 0.5525 | 1306.0 |
| 298.15 | 0.6512 | 1306.0 |
| 298.15 | 0.7494 | 1306.0 |
| 298.15 | 0.8498 | 1306.0 |
| 298.15 | 0.9541 | 1305.0 |
| 308.15 | 0.0550 | 1261.0 |
| 308.15 | 0.1509 | 1260.0 |
| 308.15 | 0.2513 | 1261.0 |
| 308.15 | 0.3489 | 1262.0 |
| 308.15 | 0.4511 | 1264.0 |
| 308.15 | 0.5015 | 1265.0 |
| 308.15 | 0.5525 | 1267.0 |
| 308.15 | 0.6512 | 1270.0 |
| 308.15 | 0.7494 | 1273.0 |
| 308.15 | 0.8498 | 1277.0 |
| 308.15 | 0.9541 | 1282.0 |