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 | 0.0530 | 0.0070 |
298.15 | 0.1049 | 0.0066 |
298.15 | 0.1670 | 0.0061 |
298.15 | 0.2004 | 0.0059 |
298.15 | 0.2561 | 0.0055 |
298.15 | 0.3039 | 0.0053 |
298.15 | 0.4046 | 0.0047 |
298.15 | 0.5013 | 0.0043 |
298.15 | 0.6004 | 0.0039 |
298.15 | 0.7009 | 0.0036 |
298.15 | 0.8027 | 0.0033 |
298.15 | 0.8520 | 0.0032 |
298.15 | 0.9007 | 0.0030 |
298.15 | 0.9512 | 0.0029 |
303.15 | 0.0530 | 0.0058 |
303.15 | 0.1049 | 0.0055 |
303.15 | 0.1670 | 0.0051 |
303.15 | 0.2004 | 0.0049 |
303.15 | 0.2561 | 0.0047 |
303.15 | 0.3039 | 0.0044 |
303.15 | 0.4046 | 0.0040 |
303.15 | 0.5013 | 0.0036 |
303.15 | 0.6004 | 0.0033 |
303.15 | 0.7009 | 0.0030 |
303.15 | 0.8027 | 0.0028 |
303.15 | 0.8520 | 0.0027 |
303.15 | 0.9007 | 0.0027 |
303.15 | 0.9512 | 0.0026 |
308.15 | 0.0530 | 0.0050 |
308.15 | 0.1049 | 0.0048 |
308.15 | 0.1670 | 0.0044 |
308.15 | 0.2004 | 0.0043 |
308.15 | 0.2561 | 0.0040 |
308.15 | 0.3039 | 0.0039 |
308.15 | 0.4046 | 0.0035 |
308.15 | 0.5013 | 0.0032 |
308.15 | 0.6004 | 0.0030 |
308.15 | 0.7009 | 0.0028 |
308.15 | 0.8027 | 0.0025 |
308.15 | 0.8520 | 0.0025 |
308.15 | 0.9007 | 0.0024 |
308.15 | 0.9512 | 0.0023 |
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 | 0.0530 | 0.0070 |
298.15 | 0.1049 | 0.0066 |
298.15 | 0.1670 | 0.0061 |
298.15 | 0.2004 | 0.0059 |
298.15 | 0.2561 | 0.0055 |
298.15 | 0.3039 | 0.0053 |
298.15 | 0.4046 | 0.0047 |
298.15 | 0.5013 | 0.0043 |
298.15 | 0.6004 | 0.0039 |
298.15 | 0.7009 | 0.0036 |
298.15 | 0.8027 | 0.0033 |
298.15 | 0.8520 | 0.0032 |
298.15 | 0.9007 | 0.0030 |
298.15 | 0.9512 | 0.0029 |
303.15 | 0.0530 | 0.0058 |
303.15 | 0.1049 | 0.0055 |
303.15 | 0.1670 | 0.0051 |
303.15 | 0.2004 | 0.0049 |
303.15 | 0.2561 | 0.0047 |
303.15 | 0.3039 | 0.0044 |
303.15 | 0.4046 | 0.0040 |
303.15 | 0.5013 | 0.0036 |
303.15 | 0.6004 | 0.0033 |
303.15 | 0.7009 | 0.0030 |
303.15 | 0.8027 | 0.0028 |
303.15 | 0.8520 | 0.0027 |
303.15 | 0.9007 | 0.0027 |
303.15 | 0.9512 | 0.0026 |
308.15 | 0.0530 | 0.0050 |
308.15 | 0.1049 | 0.0048 |
308.15 | 0.1670 | 0.0044 |
308.15 | 0.2004 | 0.0043 |
308.15 | 0.2561 | 0.0040 |
308.15 | 0.3039 | 0.0039 |
308.15 | 0.4046 | 0.0035 |
308.15 | 0.5013 | 0.0032 |
308.15 | 0.6004 | 0.0030 |
308.15 | 0.7009 | 0.0028 |
308.15 | 0.8027 | 0.0025 |
308.15 | 0.8520 | 0.0025 |
308.15 | 0.9007 | 0.0024 |
308.15 | 0.9512 | 0.0023 |
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 | 0.0530 | 828.488 |
293.15 | 0.1050 | 831.623 |
293.15 | 0.1670 | 835.443 |
293.15 | 0.2004 | 837.529 |
293.15 | 0.2561 | 841.092 |
293.15 | 0.3039 | 844.242 |
293.15 | 0.4046 | 851.133 |
293.15 | 0.5013 | 858.109 |
293.15 | 0.6004 | 865.629 |
293.15 | 0.7009 | 873.666 |
293.15 | 0.8027 | 882.262 |
293.15 | 0.8520 | 886.596 |
293.15 | 0.9007 | 891.001 |
293.15 | 0.9512 | 895.736 |
298.15 | 0.0530 | 825.018 |
298.15 | 0.1050 | 828.108 |
298.15 | 0.1670 | 831.899 |
298.15 | 0.2004 | 833.978 |
298.15 | 0.2561 | 837.535 |
298.15 | 0.3039 | 840.656 |
298.15 | 0.4046 | 847.482 |
298.15 | 0.5013 | 854.363 |
298.15 | 0.6004 | 861.773 |
298.15 | 0.7009 | 869.705 |
298.15 | 0.8027 | 878.21 |
298.15 | 0.8520 | 882.514 |
298.15 | 0.9007 | 886.89 |
298.15 | 0.9512 | 891.594 |
303.15 | 0.0530 | 821.521 |
303.15 | 0.1050 | 824.6 |
303.15 | 0.1670 | 828.337 |
303.15 | 0.2004 | 830.387 |
303.15 | 0.2561 | 833.89 |
303.15 | 0.3039 | 836.962 |
303.15 | 0.4046 | 843.721 |
303.15 | 0.5013 | 850.582 |
303.15 | 0.6004 | 857.95 |
303.15 | 0.7009 | 865.804 |
303.15 | 0.8027 | 874.181 |
303.15 | 0.8520 | 878.409 |
303.15 | 0.9007 | 882.718 |
303.15 | 0.9512 | 887.379 |
308.15 | 0.0530 | 818.004 |
308.15 | 0.1050 | 821.021 |
308.15 | 0.1670 | 824.71 |
308.15 | 0.2004 | 826.746 |
308.15 | 0.2561 | 830.229 |
308.15 | 0.3039 | 833.292 |
308.15 | 0.4046 | 839.998 |
308.15 | 0.5013 | 846.771 |
308.15 | 0.6004 | 854.07 |
308.15 | 0.7009 | 861.87 |
308.15 | 0.8027 | 870.213 |
308.15 | 0.8520 | 874.403 |
308.15 | 0.9007 | 878.687 |
308.15 | 0.9512 | 883.226 |
313.15 | 0.0530 | 814.437 |
313.15 | 0.1050 | 817.45 |
313.15 | 0.1670 | 821.134 |
313.15 | 0.2004 | 823.153 |
313.15 | 0.2561 | 826.589 |
313.15 | 0.3039 | 829.618 |
313.15 | 0.4046 | 836.231 |
313.15 | 0.5013 | 842.934 |
313.15 | 0.6004 | 850.161 |
313.15 | 0.7009 | 857.881 |
313.15 | 0.8027 | 866.131 |
313.15 | 0.8520 | 870.301 |
313.15 | 0.9007 | 874.538 |
313.15 | 0.9512 | 879.067 |
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 | 0.0530 | 828.488 |
293.15 | 0.1050 | 831.623 |
293.15 | 0.1670 | 835.443 |
293.15 | 0.2004 | 837.529 |
293.15 | 0.2561 | 841.092 |
293.15 | 0.3039 | 844.242 |
293.15 | 0.4046 | 851.133 |
293.15 | 0.5013 | 858.109 |
293.15 | 0.6004 | 865.629 |
293.15 | 0.7009 | 873.666 |
293.15 | 0.8027 | 882.262 |
293.15 | 0.8520 | 886.596 |
293.15 | 0.9007 | 891.001 |
293.15 | 0.9512 | 895.736 |
298.15 | 0.0530 | 825.018 |
298.15 | 0.1050 | 828.108 |
298.15 | 0.1670 | 831.899 |
298.15 | 0.2004 | 833.978 |
298.15 | 0.2561 | 837.535 |
298.15 | 0.3039 | 840.656 |
298.15 | 0.4046 | 847.482 |
298.15 | 0.5013 | 854.363 |
298.15 | 0.6004 | 861.773 |
298.15 | 0.7009 | 869.705 |
298.15 | 0.8027 | 878.21 |
298.15 | 0.8520 | 882.514 |
298.15 | 0.9007 | 886.89 |
298.15 | 0.9512 | 891.594 |
303.15 | 0.0530 | 821.521 |
303.15 | 0.1050 | 824.6 |
303.15 | 0.1670 | 828.337 |
303.15 | 0.2004 | 830.387 |
303.15 | 0.2561 | 833.89 |
303.15 | 0.3039 | 836.962 |
303.15 | 0.4046 | 843.721 |
303.15 | 0.5013 | 850.582 |
303.15 | 0.6004 | 857.95 |
303.15 | 0.7009 | 865.804 |
303.15 | 0.8027 | 874.181 |
303.15 | 0.8520 | 878.409 |
303.15 | 0.9007 | 882.718 |
303.15 | 0.9512 | 887.379 |
308.15 | 0.0530 | 818.004 |
308.15 | 0.1050 | 821.021 |
308.15 | 0.1670 | 824.71 |
308.15 | 0.2004 | 826.746 |
308.15 | 0.2561 | 830.229 |
308.15 | 0.3039 | 833.292 |
308.15 | 0.4046 | 839.998 |
308.15 | 0.5013 | 846.771 |
308.15 | 0.6004 | 854.07 |
308.15 | 0.7009 | 861.87 |
308.15 | 0.8027 | 870.213 |
308.15 | 0.8520 | 874.403 |
308.15 | 0.9007 | 878.687 |
308.15 | 0.9512 | 883.226 |
313.15 | 0.0530 | 814.437 |
313.15 | 0.1050 | 817.45 |
313.15 | 0.1670 | 821.134 |
313.15 | 0.2004 | 823.153 |
313.15 | 0.2561 | 826.589 |
313.15 | 0.3039 | 829.618 |
313.15 | 0.4046 | 836.231 |
313.15 | 0.5013 | 842.934 |
313.15 | 0.6004 | 850.161 |
313.15 | 0.7009 | 857.881 |
313.15 | 0.8027 | 866.131 |
313.15 | 0.8520 | 870.301 |
313.15 | 0.9007 | 874.538 |
313.15 | 0.9512 | 879.067 |
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 | 0.0530 | 1361.76 |
293.15 | 0.1050 | 1358.98 |
293.15 | 0.1670 | 1355.44 |
293.15 | 0.2004 | 1353.18 |
293.15 | 0.2561 | 1350.32 |
293.15 | 0.3039 | 1347.85 |
293.15 | 0.4046 | 1342.66 |
293.15 | 0.5013 | 1338.24 |
293.15 | 0.6004 | 1333.95 |
293.15 | 0.7009 | 1330.28 |
293.15 | 0.8027 | 1327.04 |
293.15 | 0.8520 | 1325.56 |
293.15 | 0.9007 | 1324.42 |
293.15 | 0.9512 | 1323.43 |
298.15 | 0.0530 | 1344.82 |
298.15 | 0.1050 | 1342.07 |
298.15 | 0.1670 | 1338.44 |
298.15 | 0.2004 | 1336.4 |
298.15 | 0.2561 | 1333.43 |
298.15 | 0.3039 | 1330.91 |
298.15 | 0.4046 | 1325.87 |
298.15 | 0.5013 | 1321.34 |
298.15 | 0.6004 | 1316.94 |
298.15 | 0.7009 | 1313.23 |
298.15 | 0.8027 | 1310.04 |
298.15 | 0.8520 | 1308.52 |
298.15 | 0.9007 | 1307.52 |
298.15 | 0.9512 | 1306.49 |
303.15 | 0.0530 | 1328.08 |
303.15 | 0.1050 | 1325.41 |
303.15 | 0.1670 | 1321.72 |
303.15 | 0.2004 | 1319.66 |
303.15 | 0.2561 | 1316.65 |
303.15 | 0.3039 | 1314.16 |
303.15 | 0.4046 | 1309.12 |
303.15 | 0.5013 | 1304.55 |
303.15 | 0.6004 | 1300.35 |
303.15 | 0.7009 | 1296.49 |
303.15 | 0.8027 | 1293.3 |
303.15 | 0.8520 | 1291.97 |
303.15 | 0.9007 | 1290.78 |
303.15 | 0.9512 | 1289.79 |
308.15 | 0.0530 | 1311.33 |
308.15 | 0.1050 | 1308.75 |
308.15 | 0.1670 | 1305.49 |
308.15 | 0.2004 | 1303.34 |
308.15 | 0.2561 | 1300.47 |
308.15 | 0.3039 | 1298.17 |
308.15 | 0.4046 | 1293.12 |
308.15 | 0.5013 | 1288.66 |
308.15 | 0.6004 | 1284.45 |
308.15 | 0.7009 | 1280.48 |
308.15 | 0.8027 | 1276.97 |
308.15 | 0.8520 | 1275.42 |
308.15 | 0.9007 | 1274.12 |
308.15 | 0.9512 | 1273.0 |
313.15 | 0.0530 | 1294.88 |
313.15 | 0.1050 | 1292.29 |
313.15 | 0.1670 | 1289.17 |
313.15 | 0.2004 | 1287.29 |
313.15 | 0.2561 | 1284.53 |
313.15 | 0.3039 | 1282.25 |
313.15 | 0.4046 | 1277.41 |
313.15 | 0.5013 | 1273.04 |
313.15 | 0.6004 | 1268.79 |
313.15 | 0.7009 | 1264.73 |
313.15 | 0.8027 | 1261.06 |
313.15 | 0.8520 | 1259.47 |
313.15 | 0.9007 | 1257.99 |
313.15 | 0.9512 | 1256.61 |
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 | 0.0530 | 1361.76 |
293.15 | 0.1050 | 1358.98 |
293.15 | 0.1670 | 1355.44 |
293.15 | 0.2004 | 1353.18 |
293.15 | 0.2561 | 1350.32 |
293.15 | 0.3039 | 1347.85 |
293.15 | 0.4046 | 1342.66 |
293.15 | 0.5013 | 1338.24 |
293.15 | 0.6004 | 1333.95 |
293.15 | 0.7009 | 1330.28 |
293.15 | 0.8027 | 1327.04 |
293.15 | 0.8520 | 1325.56 |
293.15 | 0.9007 | 1324.42 |
293.15 | 0.9512 | 1323.43 |
298.15 | 0.0530 | 1344.82 |
298.15 | 0.1050 | 1342.07 |
298.15 | 0.1670 | 1338.44 |
298.15 | 0.2004 | 1336.4 |
298.15 | 0.2561 | 1333.43 |
298.15 | 0.3039 | 1330.91 |
298.15 | 0.4046 | 1325.87 |
298.15 | 0.5013 | 1321.34 |
298.15 | 0.6004 | 1316.94 |
298.15 | 0.7009 | 1313.23 |
298.15 | 0.8027 | 1310.04 |
298.15 | 0.8520 | 1308.52 |
298.15 | 0.9007 | 1307.52 |
298.15 | 0.9512 | 1306.49 |
303.15 | 0.0530 | 1328.08 |
303.15 | 0.1050 | 1325.41 |
303.15 | 0.1670 | 1321.72 |
303.15 | 0.2004 | 1319.66 |
303.15 | 0.2561 | 1316.65 |
303.15 | 0.3039 | 1314.16 |
303.15 | 0.4046 | 1309.12 |
303.15 | 0.5013 | 1304.55 |
303.15 | 0.6004 | 1300.35 |
303.15 | 0.7009 | 1296.49 |
303.15 | 0.8027 | 1293.3 |
303.15 | 0.8520 | 1291.97 |
303.15 | 0.9007 | 1290.78 |
303.15 | 0.9512 | 1289.79 |
308.15 | 0.0530 | 1311.33 |
308.15 | 0.1050 | 1308.75 |
308.15 | 0.1670 | 1305.49 |
308.15 | 0.2004 | 1303.34 |
308.15 | 0.2561 | 1300.47 |
308.15 | 0.3039 | 1298.17 |
308.15 | 0.4046 | 1293.12 |
308.15 | 0.5013 | 1288.66 |
308.15 | 0.6004 | 1284.45 |
308.15 | 0.7009 | 1280.48 |
308.15 | 0.8027 | 1276.97 |
308.15 | 0.8520 | 1275.42 |
308.15 | 0.9007 | 1274.12 |
308.15 | 0.9512 | 1273.0 |
313.15 | 0.0530 | 1294.88 |
313.15 | 0.1050 | 1292.29 |
313.15 | 0.1670 | 1289.17 |
313.15 | 0.2004 | 1287.29 |
313.15 | 0.2561 | 1284.53 |
313.15 | 0.3039 | 1282.25 |
313.15 | 0.4046 | 1277.41 |
313.15 | 0.5013 | 1273.04 |
313.15 | 0.6004 | 1268.79 |
313.15 | 0.7009 | 1264.73 |
313.15 | 0.8027 | 1261.06 |
313.15 | 0.8520 | 1259.47 |
313.15 | 0.9007 | 1257.99 |
313.15 | 0.9512 | 1256.61 |