Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0535 | 0.0044 |
| 298.15 | 0.1046 | 0.0041 |
| 298.15 | 0.1546 | 0.0040 |
| 298.15 | 0.2054 | 0.0038 |
| 298.15 | 0.2530 | 0.0037 |
| 298.15 | 0.2999 | 0.0036 |
| 298.15 | 0.4044 | 0.0035 |
| 298.15 | 0.5039 | 0.0033 |
| 298.15 | 0.5932 | 0.0031 |
| 298.15 | 0.7003 | 0.0030 |
| 298.15 | 0.8019 | 0.0030 |
| 298.15 | 0.8545 | 0.0029 |
| 298.15 | 0.8987 | 0.0029 |
| 298.15 | 0.9522 | 0.0029 |
| 303.15 | 0.0535 | 0.0037 |
| 303.15 | 0.1046 | 0.0036 |
| 303.15 | 0.1546 | 0.0034 |
| 303.15 | 0.2054 | 0.0033 |
| 303.15 | 0.2530 | 0.0032 |
| 303.15 | 0.2999 | 0.0031 |
| 303.15 | 0.4044 | 0.0029 |
| 303.15 | 0.5039 | 0.0028 |
| 303.15 | 0.5932 | 0.0027 |
| 303.15 | 0.7003 | 0.0026 |
| 303.15 | 0.8019 | 0.0026 |
| 303.15 | 0.8545 | 0.0026 |
| 303.15 | 0.8987 | 0.0026 |
| 303.15 | 0.9522 | 0.0026 |
| 308.15 | 0.0535 | 0.0032 |
| 308.15 | 0.1046 | 0.0031 |
| 308.15 | 0.1546 | 0.0030 |
| 308.15 | 0.2054 | 0.0029 |
| 308.15 | 0.2530 | 0.0028 |
| 308.15 | 0.2999 | 0.0027 |
| 308.15 | 0.4044 | 0.0026 |
| 308.15 | 0.5039 | 0.0025 |
| 308.15 | 0.5932 | 0.0024 |
| 308.15 | 0.7003 | 0.0024 |
| 308.15 | 0.8019 | 0.0023 |
| 308.15 | 0.8545 | 0.0023 |
| 308.15 | 0.8987 | 0.0023 |
| 308.15 | 0.9522 | 0.0022 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0535 | 0.0044 |
| 298.15 | 0.1046 | 0.0041 |
| 298.15 | 0.1546 | 0.0040 |
| 298.15 | 0.2054 | 0.0038 |
| 298.15 | 0.2530 | 0.0037 |
| 298.15 | 0.2999 | 0.0036 |
| 298.15 | 0.4044 | 0.0035 |
| 298.15 | 0.5039 | 0.0033 |
| 298.15 | 0.5932 | 0.0031 |
| 298.15 | 0.7003 | 0.0030 |
| 298.15 | 0.8019 | 0.0030 |
| 298.15 | 0.8545 | 0.0029 |
| 298.15 | 0.8987 | 0.0029 |
| 298.15 | 0.9522 | 0.0029 |
| 303.15 | 0.0535 | 0.0037 |
| 303.15 | 0.1046 | 0.0036 |
| 303.15 | 0.1546 | 0.0034 |
| 303.15 | 0.2054 | 0.0033 |
| 303.15 | 0.2530 | 0.0032 |
| 303.15 | 0.2999 | 0.0031 |
| 303.15 | 0.4044 | 0.0029 |
| 303.15 | 0.5039 | 0.0028 |
| 303.15 | 0.5932 | 0.0027 |
| 303.15 | 0.7003 | 0.0026 |
| 303.15 | 0.8019 | 0.0026 |
| 303.15 | 0.8545 | 0.0026 |
| 303.15 | 0.8987 | 0.0026 |
| 303.15 | 0.9522 | 0.0026 |
| 308.15 | 0.0535 | 0.0032 |
| 308.15 | 0.1046 | 0.0031 |
| 308.15 | 0.1546 | 0.0030 |
| 308.15 | 0.2054 | 0.0029 |
| 308.15 | 0.2530 | 0.0028 |
| 308.15 | 0.2999 | 0.0027 |
| 308.15 | 0.4044 | 0.0026 |
| 308.15 | 0.5039 | 0.0025 |
| 308.15 | 0.5932 | 0.0024 |
| 308.15 | 0.7003 | 0.0024 |
| 308.15 | 0.8019 | 0.0023 |
| 308.15 | 0.8545 | 0.0023 |
| 308.15 | 0.8987 | 0.0023 |
| 308.15 | 0.9522 | 0.0022 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0535 | 823.637 |
| 293.15 | 0.1046 | 827.82 |
| 293.15 | 0.1546 | 831.917 |
| 293.15 | 0.2054 | 836.077 |
| 293.15 | 0.2530 | 839.982 |
| 293.15 | 0.2999 | 843.819 |
| 293.15 | 0.4044 | 852.353 |
| 293.15 | 0.5039 | 860.457 |
| 293.15 | 0.5932 | 867.724 |
| 293.15 | 0.7003 | 876.414 |
| 293.15 | 0.8019 | 884.63 |
| 293.15 | 0.8545 | 888.867 |
| 293.15 | 0.8987 | 892.418 |
| 293.15 | 0.9522 | 896.698 |
| 298.15 | 0.0535 | 820.01 |
| 298.15 | 0.1046 | 824.093 |
| 298.15 | 0.1546 | 828.161 |
| 298.15 | 0.2054 | 832.312 |
| 298.15 | 0.2530 | 836.221 |
| 298.15 | 0.2999 | 840.066 |
| 298.15 | 0.4044 | 848.606 |
| 298.15 | 0.5039 | 856.686 |
| 298.15 | 0.5932 | 863.892 |
| 298.15 | 0.7003 | 872.492 |
| 298.15 | 0.8019 | 880.623 |
| 298.15 | 0.8545 | 884.811 |
| 298.15 | 0.8987 | 888.334 |
| 298.15 | 0.9522 | 892.569 |
| 303.15 | 0.0535 | 816.368 |
| 303.15 | 0.1046 | 820.503 |
| 303.15 | 0.1546 | 824.557 |
| 303.15 | 0.2054 | 828.676 |
| 303.15 | 0.2530 | 832.536 |
| 303.15 | 0.2999 | 836.324 |
| 303.15 | 0.4044 | 844.739 |
| 303.15 | 0.5039 | 852.713 |
| 303.15 | 0.5932 | 859.852 |
| 303.15 | 0.7003 | 868.399 |
| 303.15 | 0.8019 | 876.485 |
| 303.15 | 0.8545 | 880.662 |
| 303.15 | 0.8987 | 884.162 |
| 303.15 | 0.9522 | 888.376 |
| 308.15 | 0.0535 | 812.694 |
| 308.15 | 0.1046 | 816.794 |
| 308.15 | 0.1546 | 820.816 |
| 308.15 | 0.2054 | 824.902 |
| 308.15 | 0.2530 | 828.737 |
| 308.15 | 0.2999 | 832.499 |
| 308.15 | 0.4044 | 840.855 |
| 308.15 | 0.5039 | 848.772 |
| 308.15 | 0.5932 | 855.859 |
| 308.15 | 0.7003 | 864.345 |
| 308.15 | 0.8019 | 872.393 |
| 308.15 | 0.8545 | 876.541 |
| 308.15 | 0.8987 | 880.024 |
| 308.15 | 0.9522 | 884.199 |
| 313.15 | 0.0535 | 809.018 |
| 313.15 | 0.1046 | 813.092 |
| 313.15 | 0.1546 | 817.077 |
| 313.15 | 0.2054 | 821.127 |
| 313.15 | 0.2530 | 824.921 |
| 313.15 | 0.2999 | 828.653 |
| 313.15 | 0.4044 | 836.942 |
| 313.15 | 0.5039 | 844.805 |
| 313.15 | 0.5932 | 851.852 |
| 313.15 | 0.7003 | 860.279 |
| 313.15 | 0.8019 | 868.245 |
| 313.15 | 0.8545 | 872.354 |
| 313.15 | 0.8987 | 875.803 |
| 313.15 | 0.9522 | 879.956 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0535 | 823.637 |
| 293.15 | 0.1046 | 827.82 |
| 293.15 | 0.1546 | 831.917 |
| 293.15 | 0.2054 | 836.077 |
| 293.15 | 0.2530 | 839.982 |
| 293.15 | 0.2999 | 843.819 |
| 293.15 | 0.4044 | 852.353 |
| 293.15 | 0.5039 | 860.457 |
| 293.15 | 0.5932 | 867.724 |
| 293.15 | 0.7003 | 876.414 |
| 293.15 | 0.8019 | 884.63 |
| 293.15 | 0.8545 | 888.867 |
| 293.15 | 0.8987 | 892.418 |
| 293.15 | 0.9522 | 896.698 |
| 298.15 | 0.0535 | 820.01 |
| 298.15 | 0.1046 | 824.093 |
| 298.15 | 0.1546 | 828.161 |
| 298.15 | 0.2054 | 832.312 |
| 298.15 | 0.2530 | 836.221 |
| 298.15 | 0.2999 | 840.066 |
| 298.15 | 0.4044 | 848.606 |
| 298.15 | 0.5039 | 856.686 |
| 298.15 | 0.5932 | 863.892 |
| 298.15 | 0.7003 | 872.492 |
| 298.15 | 0.8019 | 880.623 |
| 298.15 | 0.8545 | 884.811 |
| 298.15 | 0.8987 | 888.334 |
| 298.15 | 0.9522 | 892.569 |
| 303.15 | 0.0535 | 816.368 |
| 303.15 | 0.1046 | 820.503 |
| 303.15 | 0.1546 | 824.557 |
| 303.15 | 0.2054 | 828.676 |
| 303.15 | 0.2530 | 832.536 |
| 303.15 | 0.2999 | 836.324 |
| 303.15 | 0.4044 | 844.739 |
| 303.15 | 0.5039 | 852.713 |
| 303.15 | 0.5932 | 859.852 |
| 303.15 | 0.7003 | 868.399 |
| 303.15 | 0.8019 | 876.485 |
| 303.15 | 0.8545 | 880.662 |
| 303.15 | 0.8987 | 884.162 |
| 303.15 | 0.9522 | 888.376 |
| 308.15 | 0.0535 | 812.694 |
| 308.15 | 0.1046 | 816.794 |
| 308.15 | 0.1546 | 820.816 |
| 308.15 | 0.2054 | 824.902 |
| 308.15 | 0.2530 | 828.737 |
| 308.15 | 0.2999 | 832.499 |
| 308.15 | 0.4044 | 840.855 |
| 308.15 | 0.5039 | 848.772 |
| 308.15 | 0.5932 | 855.859 |
| 308.15 | 0.7003 | 864.345 |
| 308.15 | 0.8019 | 872.393 |
| 308.15 | 0.8545 | 876.541 |
| 308.15 | 0.8987 | 880.024 |
| 308.15 | 0.9522 | 884.199 |
| 313.15 | 0.0535 | 809.018 |
| 313.15 | 0.1046 | 813.092 |
| 313.15 | 0.1546 | 817.077 |
| 313.15 | 0.2054 | 821.127 |
| 313.15 | 0.2530 | 824.921 |
| 313.15 | 0.2999 | 828.653 |
| 313.15 | 0.4044 | 836.942 |
| 313.15 | 0.5039 | 844.805 |
| 313.15 | 0.5932 | 851.852 |
| 313.15 | 0.7003 | 860.279 |
| 313.15 | 0.8019 | 868.245 |
| 313.15 | 0.8545 | 872.354 |
| 313.15 | 0.8987 | 875.803 |
| 313.15 | 0.9522 | 879.956 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0535 | 1319.98 |
| 293.15 | 0.1046 | 1319.4 |
| 293.15 | 0.1546 | 1319.1 |
| 293.15 | 0.2054 | 1318.77 |
| 293.15 | 0.2530 | 1318.51 |
| 293.15 | 0.2999 | 1318.32 |
| 293.15 | 0.4044 | 1318.28 |
| 293.15 | 0.5039 | 1318.48 |
| 293.15 | 0.5932 | 1318.86 |
| 293.15 | 0.7003 | 1319.64 |
| 293.15 | 0.8019 | 1320.73 |
| 293.15 | 0.8545 | 1321.36 |
| 293.15 | 0.8987 | 1322.01 |
| 293.15 | 0.9522 | 1322.76 |
| 298.15 | 0.0535 | 1303.1 |
| 298.15 | 0.1046 | 1302.58 |
| 298.15 | 0.1546 | 1302.16 |
| 298.15 | 0.2054 | 1301.85 |
| 298.15 | 0.2530 | 1301.6 |
| 298.15 | 0.2999 | 1301.37 |
| 298.15 | 0.4044 | 1301.28 |
| 298.15 | 0.5039 | 1301.46 |
| 298.15 | 0.5932 | 1301.85 |
| 298.15 | 0.7003 | 1302.56 |
| 298.15 | 0.8019 | 1303.62 |
| 298.15 | 0.8545 | 1304.35 |
| 298.15 | 0.8987 | 1304.96 |
| 298.15 | 0.9522 | 1305.67 |
| 303.15 | 0.0535 | 1286.31 |
| 303.15 | 0.1046 | 1285.77 |
| 303.15 | 0.1546 | 1285.49 |
| 303.15 | 0.2054 | 1285.16 |
| 303.15 | 0.2530 | 1284.91 |
| 303.15 | 0.2999 | 1284.77 |
| 303.15 | 0.4044 | 1284.65 |
| 303.15 | 0.5039 | 1284.82 |
| 303.15 | 0.5932 | 1285.17 |
| 303.15 | 0.7003 | 1285.86 |
| 303.15 | 0.8019 | 1286.81 |
| 303.15 | 0.8545 | 1287.39 |
| 303.15 | 0.8987 | 1287.98 |
| 303.15 | 0.9522 | 1288.67 |
| 308.15 | 0.0535 | 1269.64 |
| 308.15 | 0.1046 | 1269.19 |
| 308.15 | 0.1546 | 1268.85 |
| 308.15 | 0.2054 | 1268.56 |
| 308.15 | 0.2530 | 1268.3 |
| 308.15 | 0.2999 | 1268.18 |
| 308.15 | 0.4044 | 1268.06 |
| 308.15 | 0.5039 | 1268.21 |
| 308.15 | 0.5932 | 1268.59 |
| 308.15 | 0.7003 | 1269.25 |
| 308.15 | 0.8019 | 1270.1 |
| 308.15 | 0.8545 | 1270.59 |
| 308.15 | 0.8987 | 1271.1 |
| 308.15 | 0.9522 | 1271.77 |
| 313.15 | 0.0535 | 1253.04 |
| 313.15 | 0.1046 | 1252.67 |
| 313.15 | 0.1546 | 1252.41 |
| 313.15 | 0.2054 | 1252.17 |
| 313.15 | 0.2530 | 1252.0 |
| 313.15 | 0.2999 | 1251.88 |
| 313.15 | 0.4044 | 1251.77 |
| 313.15 | 0.5039 | 1251.89 |
| 313.15 | 0.5932 | 1252.17 |
| 313.15 | 0.7003 | 1252.72 |
| 313.15 | 0.8019 | 1253.41 |
| 313.15 | 0.8545 | 1253.89 |
| 313.15 | 0.8987 | 1254.28 |
| 313.15 | 0.9522 | 1254.87 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0535 | 1319.98 |
| 293.15 | 0.1046 | 1319.4 |
| 293.15 | 0.1546 | 1319.1 |
| 293.15 | 0.2054 | 1318.77 |
| 293.15 | 0.2530 | 1318.51 |
| 293.15 | 0.2999 | 1318.32 |
| 293.15 | 0.4044 | 1318.28 |
| 293.15 | 0.5039 | 1318.48 |
| 293.15 | 0.5932 | 1318.86 |
| 293.15 | 0.7003 | 1319.64 |
| 293.15 | 0.8019 | 1320.73 |
| 293.15 | 0.8545 | 1321.36 |
| 293.15 | 0.8987 | 1322.01 |
| 293.15 | 0.9522 | 1322.76 |
| 298.15 | 0.0535 | 1303.1 |
| 298.15 | 0.1046 | 1302.58 |
| 298.15 | 0.1546 | 1302.16 |
| 298.15 | 0.2054 | 1301.85 |
| 298.15 | 0.2530 | 1301.6 |
| 298.15 | 0.2999 | 1301.37 |
| 298.15 | 0.4044 | 1301.28 |
| 298.15 | 0.5039 | 1301.46 |
| 298.15 | 0.5932 | 1301.85 |
| 298.15 | 0.7003 | 1302.56 |
| 298.15 | 0.8019 | 1303.62 |
| 298.15 | 0.8545 | 1304.35 |
| 298.15 | 0.8987 | 1304.96 |
| 298.15 | 0.9522 | 1305.67 |
| 303.15 | 0.0535 | 1286.31 |
| 303.15 | 0.1046 | 1285.77 |
| 303.15 | 0.1546 | 1285.49 |
| 303.15 | 0.2054 | 1285.16 |
| 303.15 | 0.2530 | 1284.91 |
| 303.15 | 0.2999 | 1284.77 |
| 303.15 | 0.4044 | 1284.65 |
| 303.15 | 0.5039 | 1284.82 |
| 303.15 | 0.5932 | 1285.17 |
| 303.15 | 0.7003 | 1285.86 |
| 303.15 | 0.8019 | 1286.81 |
| 303.15 | 0.8545 | 1287.39 |
| 303.15 | 0.8987 | 1287.98 |
| 303.15 | 0.9522 | 1288.67 |
| 308.15 | 0.0535 | 1269.64 |
| 308.15 | 0.1046 | 1269.19 |
| 308.15 | 0.1546 | 1268.85 |
| 308.15 | 0.2054 | 1268.56 |
| 308.15 | 0.2530 | 1268.3 |
| 308.15 | 0.2999 | 1268.18 |
| 308.15 | 0.4044 | 1268.06 |
| 308.15 | 0.5039 | 1268.21 |
| 308.15 | 0.5932 | 1268.59 |
| 308.15 | 0.7003 | 1269.25 |
| 308.15 | 0.8019 | 1270.1 |
| 308.15 | 0.8545 | 1270.59 |
| 308.15 | 0.8987 | 1271.1 |
| 308.15 | 0.9522 | 1271.77 |
| 313.15 | 0.0535 | 1253.04 |
| 313.15 | 0.1046 | 1252.67 |
| 313.15 | 0.1546 | 1252.41 |
| 313.15 | 0.2054 | 1252.17 |
| 313.15 | 0.2530 | 1252.0 |
| 313.15 | 0.2999 | 1251.88 |
| 313.15 | 0.4044 | 1251.77 |
| 313.15 | 0.5039 | 1251.89 |
| 313.15 | 0.5932 | 1252.17 |
| 313.15 | 0.7003 | 1252.72 |
| 313.15 | 0.8019 | 1253.41 |
| 313.15 | 0.8545 | 1253.89 |
| 313.15 | 0.8987 | 1254.28 |
| 313.15 | 0.9522 | 1254.87 |