Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1085 | 837.518 |
288.15 | 0.1608 | 848.615 |
288.15 | 0.2102 | 857.751 |
288.15 | 0.2477 | 863.891 |
288.15 | 0.2972 | 871.227 |
288.15 | 0.3493 | 878.129 |
288.15 | 0.4048 | 884.6 |
288.15 | 0.4600 | 890.404 |
288.15 | 0.5003 | 894.261 |
288.15 | 0.5584 | 899.282 |
288.15 | 0.6066 | 903.088 |
288.15 | 0.6604 | 906.948 |
288.15 | 0.6964 | 909.32 |
288.15 | 0.7532 | 912.745 |
288.15 | 0.8054 | 915.595 |
288.15 | 0.8563 | 918.152 |
288.15 | 0.9044 | 920.357 |
288.15 | 0.9593 | 922.69 |
298.15 | 0.1085 | 829.325 |
298.15 | 0.1608 | 840.381 |
298.15 | 0.2102 | 849.425 |
298.15 | 0.2477 | 855.521 |
298.15 | 0.2972 | 862.829 |
298.15 | 0.3493 | 869.65 |
298.15 | 0.4048 | 876.088 |
298.15 | 0.4600 | 881.84 |
298.15 | 0.5003 | 885.64 |
298.15 | 0.5584 | 890.668 |
298.15 | 0.6066 | 894.428 |
298.15 | 0.6604 | 898.225 |
298.15 | 0.6964 | 900.561 |
298.15 | 0.7532 | 903.981 |
298.15 | 0.8054 | 906.826 |
298.15 | 0.8563 | 909.394 |
298.15 | 0.9044 | 911.598 |
298.15 | 0.9593 | 913.937 |
308.15 | 0.1085 | 820.919 |
308.15 | 0.1608 | 831.968 |
308.15 | 0.2102 | 841.022 |
308.15 | 0.2477 | 847.161 |
308.15 | 0.2972 | 854.397 |
308.15 | 0.3493 | 861.101 |
308.15 | 0.4048 | 867.464 |
308.15 | 0.4600 | 873.153 |
308.15 | 0.5003 | 876.925 |
308.15 | 0.5584 | 881.873 |
308.15 | 0.6066 | 885.633 |
308.15 | 0.6604 | 889.461 |
308.15 | 0.6964 | 891.847 |
308.15 | 0.7532 | 895.267 |
308.15 | 0.8054 | 898.1 |
308.15 | 0.8563 | 900.587 |
308.15 | 0.9044 | 902.735 |
308.15 | 0.9593 | 905.015 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1062 | 843.052 |
288.15 | 0.1678 | 856.676 |
288.15 | 0.2147 | 865.458 |
288.15 | 0.2748 | 875.451 |
288.15 | 0.3074 | 880.428 |
288.15 | 0.3594 | 887.763 |
288.15 | 0.4007 | 893.137 |
288.15 | 0.4540 | 899.478 |
288.15 | 0.5065 | 905.116 |
288.15 | 0.5476 | 909.104 |
288.15 | 0.6141 | 914.857 |
288.15 | 0.6648 | 918.787 |
288.15 | 0.7057 | 921.697 |
288.15 | 0.7615 | 925.378 |
288.15 | 0.8008 | 927.797 |
288.15 | 0.8663 | 931.55 |
288.15 | 0.9129 | 933.87 |
288.15 | 0.9611 | 935.832 |
293.15 | 0.1062 | 839.34 |
293.15 | 0.1678 | 852.869 |
293.15 | 0.2147 | 861.572 |
293.15 | 0.2748 | 871.495 |
293.15 | 0.3074 | 876.423 |
293.15 | 0.3594 | 883.755 |
293.15 | 0.4007 | 889.131 |
293.15 | 0.4540 | 895.473 |
293.15 | 0.5065 | 901.108 |
293.15 | 0.5476 | 905.089 |
293.15 | 0.6141 | 910.869 |
293.15 | 0.6648 | 914.772 |
293.15 | 0.7057 | 917.7 |
293.15 | 0.7615 | 921.402 |
293.15 | 0.8008 | 923.841 |
293.15 | 0.8663 | 927.598 |
293.15 | 0.9129 | 929.946 |
293.15 | 0.9611 | 931.895 |
298.15 | 0.1062 | 835.067 |
298.15 | 0.1678 | 848.695 |
298.15 | 0.2147 | 857.456 |
298.15 | 0.2748 | 867.42 |
298.15 | 0.3074 | 872.391 |
298.15 | 0.3594 | 879.735 |
298.15 | 0.4007 | 885.109 |
298.15 | 0.4540 | 891.458 |
298.15 | 0.5065 | 897.101 |
298.15 | 0.5476 | 901.088 |
298.15 | 0.6141 | 906.849 |
298.15 | 0.6648 | 910.769 |
298.15 | 0.7057 | 913.696 |
298.15 | 0.7615 | 917.412 |
298.15 | 0.8008 | 919.869 |
298.15 | 0.8663 | 923.643 |
298.15 | 0.9129 | 925.995 |
298.15 | 0.9611 | 927.934 |
303.15 | 0.1062 | 831.089 |
303.15 | 0.1678 | 844.674 |
303.15 | 0.2147 | 853.42 |
303.15 | 0.2748 | 863.377 |
303.15 | 0.3074 | 868.329 |
303.15 | 0.3594 | 875.695 |
303.15 | 0.4007 | 881.072 |
303.15 | 0.4540 | 887.425 |
303.15 | 0.5065 | 893.072 |
303.15 | 0.5476 | 897.062 |
303.15 | 0.6141 | 902.826 |
303.15 | 0.6648 | 906.756 |
303.15 | 0.7057 | 909.679 |
303.15 | 0.7615 | 913.4 |
303.15 | 0.8008 | 915.862 |
303.15 | 0.8663 | 919.659 |
303.15 | 0.9129 | 922.009 |
303.15 | 0.9611 | 923.955 |
308.15 | 0.1062 | 827.206 |
308.15 | 0.1678 | 840.696 |
308.15 | 0.2147 | 849.384 |
308.15 | 0.2748 | 859.316 |
308.15 | 0.3074 | 864.284 |
308.15 | 0.3594 | 871.64 |
308.15 | 0.4007 | 877.016 |
308.15 | 0.4540 | 883.38 |
308.15 | 0.5065 | 889.029 |
308.15 | 0.5476 | 893.028 |
308.15 | 0.6141 | 898.797 |
308.15 | 0.6648 | 902.724 |
308.15 | 0.7057 | 905.653 |
308.15 | 0.7615 | 909.372 |
308.15 | 0.8008 | 911.828 |
308.15 | 0.8663 | 915.63 |
308.15 | 0.9129 | 918.002 |
308.15 | 0.9611 | 919.943 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1085 | 837.518 |
288.15 | 0.1608 | 848.615 |
288.15 | 0.2102 | 857.751 |
288.15 | 0.2477 | 863.891 |
288.15 | 0.2972 | 871.227 |
288.15 | 0.3493 | 878.129 |
288.15 | 0.4048 | 884.6 |
288.15 | 0.4600 | 890.404 |
288.15 | 0.5003 | 894.261 |
288.15 | 0.5584 | 899.282 |
288.15 | 0.6066 | 903.088 |
288.15 | 0.6604 | 906.948 |
288.15 | 0.6964 | 909.32 |
288.15 | 0.7532 | 912.745 |
288.15 | 0.8054 | 915.595 |
288.15 | 0.8563 | 918.152 |
288.15 | 0.9044 | 920.357 |
288.15 | 0.9593 | 922.69 |
298.15 | 0.1085 | 829.325 |
298.15 | 0.1608 | 840.381 |
298.15 | 0.2102 | 849.425 |
298.15 | 0.2477 | 855.521 |
298.15 | 0.2972 | 862.829 |
298.15 | 0.3493 | 869.65 |
298.15 | 0.4048 | 876.088 |
298.15 | 0.4600 | 881.84 |
298.15 | 0.5003 | 885.64 |
298.15 | 0.5584 | 890.668 |
298.15 | 0.6066 | 894.428 |
298.15 | 0.6604 | 898.225 |
298.15 | 0.6964 | 900.561 |
298.15 | 0.7532 | 903.981 |
298.15 | 0.8054 | 906.826 |
298.15 | 0.8563 | 909.394 |
298.15 | 0.9044 | 911.598 |
298.15 | 0.9593 | 913.937 |
308.15 | 0.1085 | 820.919 |
308.15 | 0.1608 | 831.968 |
308.15 | 0.2102 | 841.022 |
308.15 | 0.2477 | 847.161 |
308.15 | 0.2972 | 854.397 |
308.15 | 0.3493 | 861.101 |
308.15 | 0.4048 | 867.464 |
308.15 | 0.4600 | 873.153 |
308.15 | 0.5003 | 876.925 |
308.15 | 0.5584 | 881.873 |
308.15 | 0.6066 | 885.633 |
308.15 | 0.6604 | 889.461 |
308.15 | 0.6964 | 891.847 |
308.15 | 0.7532 | 895.267 |
308.15 | 0.8054 | 898.1 |
308.15 | 0.8563 | 900.587 |
308.15 | 0.9044 | 902.735 |
308.15 | 0.9593 | 905.015 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1062 | 843.052 |
288.15 | 0.1678 | 856.676 |
288.15 | 0.2147 | 865.458 |
288.15 | 0.2748 | 875.451 |
288.15 | 0.3074 | 880.428 |
288.15 | 0.3594 | 887.763 |
288.15 | 0.4007 | 893.137 |
288.15 | 0.4540 | 899.478 |
288.15 | 0.5065 | 905.116 |
288.15 | 0.5476 | 909.104 |
288.15 | 0.6141 | 914.857 |
288.15 | 0.6648 | 918.787 |
288.15 | 0.7057 | 921.697 |
288.15 | 0.7615 | 925.378 |
288.15 | 0.8008 | 927.797 |
288.15 | 0.8663 | 931.55 |
288.15 | 0.9129 | 933.87 |
288.15 | 0.9611 | 935.832 |
293.15 | 0.1062 | 839.34 |
293.15 | 0.1678 | 852.869 |
293.15 | 0.2147 | 861.572 |
293.15 | 0.2748 | 871.495 |
293.15 | 0.3074 | 876.423 |
293.15 | 0.3594 | 883.755 |
293.15 | 0.4007 | 889.131 |
293.15 | 0.4540 | 895.473 |
293.15 | 0.5065 | 901.108 |
293.15 | 0.5476 | 905.089 |
293.15 | 0.6141 | 910.869 |
293.15 | 0.6648 | 914.772 |
293.15 | 0.7057 | 917.7 |
293.15 | 0.7615 | 921.402 |
293.15 | 0.8008 | 923.841 |
293.15 | 0.8663 | 927.598 |
293.15 | 0.9129 | 929.946 |
293.15 | 0.9611 | 931.895 |
298.15 | 0.1062 | 835.067 |
298.15 | 0.1678 | 848.695 |
298.15 | 0.2147 | 857.456 |
298.15 | 0.2748 | 867.42 |
298.15 | 0.3074 | 872.391 |
298.15 | 0.3594 | 879.735 |
298.15 | 0.4007 | 885.109 |
298.15 | 0.4540 | 891.458 |
298.15 | 0.5065 | 897.101 |
298.15 | 0.5476 | 901.088 |
298.15 | 0.6141 | 906.849 |
298.15 | 0.6648 | 910.769 |
298.15 | 0.7057 | 913.696 |
298.15 | 0.7615 | 917.412 |
298.15 | 0.8008 | 919.869 |
298.15 | 0.8663 | 923.643 |
298.15 | 0.9129 | 925.995 |
298.15 | 0.9611 | 927.934 |
303.15 | 0.1062 | 831.089 |
303.15 | 0.1678 | 844.674 |
303.15 | 0.2147 | 853.42 |
303.15 | 0.2748 | 863.377 |
303.15 | 0.3074 | 868.329 |
303.15 | 0.3594 | 875.695 |
303.15 | 0.4007 | 881.072 |
303.15 | 0.4540 | 887.425 |
303.15 | 0.5065 | 893.072 |
303.15 | 0.5476 | 897.062 |
303.15 | 0.6141 | 902.826 |
303.15 | 0.6648 | 906.756 |
303.15 | 0.7057 | 909.679 |
303.15 | 0.7615 | 913.4 |
303.15 | 0.8008 | 915.862 |
303.15 | 0.8663 | 919.659 |
303.15 | 0.9129 | 922.009 |
303.15 | 0.9611 | 923.955 |
308.15 | 0.1062 | 827.206 |
308.15 | 0.1678 | 840.696 |
308.15 | 0.2147 | 849.384 |
308.15 | 0.2748 | 859.316 |
308.15 | 0.3074 | 864.284 |
308.15 | 0.3594 | 871.64 |
308.15 | 0.4007 | 877.016 |
308.15 | 0.4540 | 883.38 |
308.15 | 0.5065 | 889.029 |
308.15 | 0.5476 | 893.028 |
308.15 | 0.6141 | 898.797 |
308.15 | 0.6648 | 902.724 |
308.15 | 0.7057 | 905.653 |
308.15 | 0.7615 | 909.372 |
308.15 | 0.8008 | 911.828 |
308.15 | 0.8663 | 915.63 |
308.15 | 0.9129 | 918.002 |
308.15 | 0.9611 | 919.943 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Speed of sound, m/s - Liquid |
288.15 | 0.1062 | 1284.22 |
288.15 | 0.1678 | 1301.99 |
288.15 | 0.2147 | 1313.7 |
288.15 | 0.2748 | 1327.19 |
288.15 | 0.3074 | 1333.75 |
288.15 | 0.3594 | 1343.29 |
288.15 | 0.4007 | 1350.05 |
288.15 | 0.4540 | 1357.9 |
288.15 | 0.5065 | 1364.8 |
288.15 | 0.5476 | 1369.75 |
288.15 | 0.6141 | 1376.84 |
288.15 | 0.6648 | 1381.92 |
288.15 | 0.7057 | 1385.42 |
288.15 | 0.7615 | 1389.94 |
288.15 | 0.8008 | 1392.91 |
288.15 | 0.8663 | 1397.41 |
288.15 | 0.9129 | 1400.26 |
288.15 | 0.9611 | 1402.93 |
293.15 | 0.1062 | 1267.34 |
293.15 | 0.1678 | 1284.56 |
293.15 | 0.2147 | 1296.26 |
293.15 | 0.2748 | 1309.65 |
293.15 | 0.3074 | 1316.35 |
293.15 | 0.3594 | 1326.02 |
293.15 | 0.4007 | 1332.9 |
293.15 | 0.4540 | 1340.94 |
293.15 | 0.5065 | 1348.06 |
293.15 | 0.5476 | 1353.11 |
293.15 | 0.6141 | 1360.22 |
293.15 | 0.6648 | 1365.06 |
293.15 | 0.7057 | 1368.6 |
293.15 | 0.7615 | 1372.95 |
293.15 | 0.8008 | 1375.88 |
293.15 | 0.8663 | 1380.32 |
293.15 | 0.9129 | 1383.37 |
293.15 | 0.9611 | 1386.38 |
298.15 | 0.1062 | 1249.32 |
298.15 | 0.1678 | 1267.64 |
298.15 | 0.2147 | 1279.74 |
298.15 | 0.2748 | 1293.36 |
298.15 | 0.3074 | 1299.91 |
298.15 | 0.3594 | 1309.31 |
298.15 | 0.4007 | 1316.04 |
298.15 | 0.4540 | 1323.95 |
298.15 | 0.5065 | 1330.8 |
298.15 | 0.5476 | 1335.82 |
298.15 | 0.6141 | 1343.05 |
298.15 | 0.6648 | 1348.1 |
298.15 | 0.7057 | 1351.84 |
298.15 | 0.7615 | 1356.56 |
298.15 | 0.8008 | 1359.53 |
298.15 | 0.8663 | 1363.92 |
298.15 | 0.9129 | 1366.51 |
298.15 | 0.9611 | 1368.72 |
303.15 | 0.1062 | 1232.64 |
303.15 | 0.1678 | 1250.96 |
303.15 | 0.2147 | 1262.96 |
303.15 | 0.2748 | 1276.42 |
303.15 | 0.3074 | 1282.96 |
303.15 | 0.3594 | 1292.35 |
303.15 | 0.4007 | 1299.0 |
303.15 | 0.4540 | 1306.91 |
303.15 | 0.5065 | 1313.86 |
303.15 | 0.5476 | 1318.84 |
303.15 | 0.6141 | 1326.22 |
303.15 | 0.6648 | 1331.38 |
303.15 | 0.7057 | 1335.15 |
303.15 | 0.7615 | 1339.89 |
303.15 | 0.8008 | 1342.88 |
303.15 | 0.8663 | 1347.24 |
303.15 | 0.9129 | 1349.8 |
303.15 | 0.9611 | 1351.8 |
308.15 | 0.1062 | 1215.78 |
308.15 | 0.1678 | 1233.96 |
308.15 | 0.2147 | 1245.99 |
308.15 | 0.2748 | 1259.48 |
308.15 | 0.3074 | 1266.02 |
308.15 | 0.3594 | 1275.53 |
308.15 | 0.4007 | 1282.27 |
308.15 | 0.4540 | 1290.14 |
308.15 | 0.5065 | 1297.1 |
308.15 | 0.5476 | 1302.1 |
308.15 | 0.6141 | 1309.36 |
308.15 | 0.6648 | 1314.35 |
308.15 | 0.7057 | 1318.07 |
308.15 | 0.7615 | 1322.75 |
308.15 | 0.8008 | 1325.81 |
308.15 | 0.8663 | 1330.19 |
308.15 | 0.9129 | 1332.92 |
308.15 | 0.9611 | 1335.33 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Speed of sound, m/s - Liquid |
288.15 | 0.1062 | 1284.22 |
288.15 | 0.1678 | 1301.99 |
288.15 | 0.2147 | 1313.7 |
288.15 | 0.2748 | 1327.19 |
288.15 | 0.3074 | 1333.75 |
288.15 | 0.3594 | 1343.29 |
288.15 | 0.4007 | 1350.05 |
288.15 | 0.4540 | 1357.9 |
288.15 | 0.5065 | 1364.8 |
288.15 | 0.5476 | 1369.75 |
288.15 | 0.6141 | 1376.84 |
288.15 | 0.6648 | 1381.92 |
288.15 | 0.7057 | 1385.42 |
288.15 | 0.7615 | 1389.94 |
288.15 | 0.8008 | 1392.91 |
288.15 | 0.8663 | 1397.41 |
288.15 | 0.9129 | 1400.26 |
288.15 | 0.9611 | 1402.93 |
293.15 | 0.1062 | 1267.34 |
293.15 | 0.1678 | 1284.56 |
293.15 | 0.2147 | 1296.26 |
293.15 | 0.2748 | 1309.65 |
293.15 | 0.3074 | 1316.35 |
293.15 | 0.3594 | 1326.02 |
293.15 | 0.4007 | 1332.9 |
293.15 | 0.4540 | 1340.94 |
293.15 | 0.5065 | 1348.06 |
293.15 | 0.5476 | 1353.11 |
293.15 | 0.6141 | 1360.22 |
293.15 | 0.6648 | 1365.06 |
293.15 | 0.7057 | 1368.6 |
293.15 | 0.7615 | 1372.95 |
293.15 | 0.8008 | 1375.88 |
293.15 | 0.8663 | 1380.32 |
293.15 | 0.9129 | 1383.37 |
293.15 | 0.9611 | 1386.38 |
298.15 | 0.1062 | 1249.32 |
298.15 | 0.1678 | 1267.64 |
298.15 | 0.2147 | 1279.74 |
298.15 | 0.2748 | 1293.36 |
298.15 | 0.3074 | 1299.91 |
298.15 | 0.3594 | 1309.31 |
298.15 | 0.4007 | 1316.04 |
298.15 | 0.4540 | 1323.95 |
298.15 | 0.5065 | 1330.8 |
298.15 | 0.5476 | 1335.82 |
298.15 | 0.6141 | 1343.05 |
298.15 | 0.6648 | 1348.1 |
298.15 | 0.7057 | 1351.84 |
298.15 | 0.7615 | 1356.56 |
298.15 | 0.8008 | 1359.53 |
298.15 | 0.8663 | 1363.92 |
298.15 | 0.9129 | 1366.51 |
298.15 | 0.9611 | 1368.72 |
303.15 | 0.1062 | 1232.64 |
303.15 | 0.1678 | 1250.96 |
303.15 | 0.2147 | 1262.96 |
303.15 | 0.2748 | 1276.42 |
303.15 | 0.3074 | 1282.96 |
303.15 | 0.3594 | 1292.35 |
303.15 | 0.4007 | 1299.0 |
303.15 | 0.4540 | 1306.91 |
303.15 | 0.5065 | 1313.86 |
303.15 | 0.5476 | 1318.84 |
303.15 | 0.6141 | 1326.22 |
303.15 | 0.6648 | 1331.38 |
303.15 | 0.7057 | 1335.15 |
303.15 | 0.7615 | 1339.89 |
303.15 | 0.8008 | 1342.88 |
303.15 | 0.8663 | 1347.24 |
303.15 | 0.9129 | 1349.8 |
303.15 | 0.9611 | 1351.8 |
308.15 | 0.1062 | 1215.78 |
308.15 | 0.1678 | 1233.96 |
308.15 | 0.2147 | 1245.99 |
308.15 | 0.2748 | 1259.48 |
308.15 | 0.3074 | 1266.02 |
308.15 | 0.3594 | 1275.53 |
308.15 | 0.4007 | 1282.27 |
308.15 | 0.4540 | 1290.14 |
308.15 | 0.5065 | 1297.1 |
308.15 | 0.5476 | 1302.1 |
308.15 | 0.6141 | 1309.36 |
308.15 | 0.6648 | 1314.35 |
308.15 | 0.7057 | 1318.07 |
308.15 | 0.7615 | 1322.75 |
308.15 | 0.8008 | 1325.81 |
308.15 | 0.8663 | 1330.19 |
308.15 | 0.9129 | 1332.92 |
308.15 | 0.9611 | 1335.33 |