Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.1168 | 288.15 | 797.427 |
0.1168 | 293.15 | 793.696 |
0.1168 | 298.15 | 789.759 |
0.1168 | 303.15 | 785.812 |
0.1168 | 308.15 | 782.055 |
0.1659 | 288.15 | 804.49 |
0.1659 | 293.15 | 800.716 |
0.1659 | 298.15 | 796.756 |
0.1659 | 303.15 | 792.8 |
0.1659 | 308.15 | 788.975 |
0.2092 | 288.15 | 810.815 |
0.2092 | 293.15 | 806.993 |
0.2092 | 298.15 | 803.027 |
0.2092 | 303.15 | 799.078 |
0.2092 | 308.15 | 795.2 |
0.2589 | 288.15 | 818.158 |
0.2589 | 293.15 | 814.291 |
0.2589 | 298.15 | 810.334 |
0.2589 | 303.15 | 806.371 |
0.2589 | 308.15 | 802.458 |
0.3155 | 288.15 | 826.596 |
0.3155 | 293.15 | 822.69 |
0.3155 | 298.15 | 818.738 |
0.3155 | 303.15 | 814.795 |
0.3155 | 308.15 | 810.825 |
0.3564 | 288.15 | 832.755 |
0.3564 | 293.15 | 828.829 |
0.3564 | 298.15 | 824.867 |
0.3564 | 303.15 | 820.924 |
0.3564 | 308.15 | 816.944 |
0.3830 | 288.15 | 836.791 |
0.3830 | 293.15 | 832.842 |
0.3830 | 298.15 | 828.881 |
0.3830 | 303.15 | 824.93 |
0.3830 | 308.15 | 820.957 |
0.4544 | 288.15 | 847.683 |
0.4544 | 293.15 | 843.729 |
0.4544 | 298.15 | 839.761 |
0.4544 | 303.15 | 835.783 |
0.4544 | 308.15 | 831.821 |
0.5108 | 288.15 | 856.418 |
0.5108 | 293.15 | 852.463 |
0.5108 | 298.15 | 848.467 |
0.5108 | 303.15 | 844.479 |
0.5108 | 308.15 | 840.528 |
0.5568 | 288.15 | 863.63 |
0.5568 | 293.15 | 859.691 |
0.5568 | 298.15 | 855.668 |
0.5568 | 303.15 | 851.665 |
0.5568 | 308.15 | 847.701 |
0.6107 | 288.15 | 872.206 |
0.6107 | 293.15 | 868.299 |
0.6107 | 298.15 | 864.217 |
0.6107 | 303.15 | 860.198 |
0.6107 | 308.15 | 856.228 |
0.6683 | 288.15 | 881.543 |
0.6683 | 293.15 | 877.641 |
0.6683 | 298.15 | 873.531 |
0.6683 | 303.15 | 869.475 |
0.6683 | 308.15 | 865.486 |
0.6924 | 288.15 | 885.505 |
0.6924 | 293.15 | 881.587 |
0.6924 | 298.15 | 877.468 |
0.6924 | 303.15 | 873.41 |
0.6924 | 308.15 | 869.396 |
0.7544 | 288.15 | 895.808 |
0.7544 | 293.15 | 891.893 |
0.7544 | 298.15 | 887.746 |
0.7544 | 303.15 | 883.674 |
0.7544 | 308.15 | 879.592 |
0.7963 | 288.15 | 902.873 |
0.7963 | 293.15 | 898.935 |
0.7963 | 298.15 | 894.791 |
0.7963 | 303.15 | 890.73 |
0.7963 | 308.15 | 886.574 |
0.8580 | 288.15 | 913.335 |
0.8580 | 293.15 | 909.366 |
0.8580 | 298.15 | 905.245 |
0.8580 | 303.15 | 901.206 |
0.8580 | 308.15 | 896.983 |
0.9079 | 288.15 | 921.784 |
0.9079 | 293.15 | 917.773 |
0.9079 | 298.15 | 913.7 |
0.9079 | 303.15 | 909.674 |
0.9079 | 308.15 | 905.434 |
0.9553 | 288.15 | 929.676 |
0.9553 | 293.15 | 925.674 |
0.9553 | 298.15 | 921.63 |
0.9553 | 303.15 | 917.622 |
0.9553 | 308.15 | 913.46 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.1168 | 288.15 | 797.427 |
0.1168 | 293.15 | 793.696 |
0.1168 | 298.15 | 789.759 |
0.1168 | 303.15 | 785.812 |
0.1168 | 308.15 | 782.055 |
0.1659 | 288.15 | 804.49 |
0.1659 | 293.15 | 800.716 |
0.1659 | 298.15 | 796.756 |
0.1659 | 303.15 | 792.8 |
0.1659 | 308.15 | 788.975 |
0.2092 | 288.15 | 810.815 |
0.2092 | 293.15 | 806.993 |
0.2092 | 298.15 | 803.027 |
0.2092 | 303.15 | 799.078 |
0.2092 | 308.15 | 795.2 |
0.2589 | 288.15 | 818.158 |
0.2589 | 293.15 | 814.291 |
0.2589 | 298.15 | 810.334 |
0.2589 | 303.15 | 806.371 |
0.2589 | 308.15 | 802.458 |
0.3155 | 288.15 | 826.596 |
0.3155 | 293.15 | 822.69 |
0.3155 | 298.15 | 818.738 |
0.3155 | 303.15 | 814.795 |
0.3155 | 308.15 | 810.825 |
0.3564 | 288.15 | 832.755 |
0.3564 | 293.15 | 828.829 |
0.3564 | 298.15 | 824.867 |
0.3564 | 303.15 | 820.924 |
0.3564 | 308.15 | 816.944 |
0.3830 | 288.15 | 836.791 |
0.3830 | 293.15 | 832.842 |
0.3830 | 298.15 | 828.881 |
0.3830 | 303.15 | 824.93 |
0.3830 | 308.15 | 820.957 |
0.4544 | 288.15 | 847.683 |
0.4544 | 293.15 | 843.729 |
0.4544 | 298.15 | 839.761 |
0.4544 | 303.15 | 835.783 |
0.4544 | 308.15 | 831.821 |
0.5108 | 288.15 | 856.418 |
0.5108 | 293.15 | 852.463 |
0.5108 | 298.15 | 848.467 |
0.5108 | 303.15 | 844.479 |
0.5108 | 308.15 | 840.528 |
0.5568 | 288.15 | 863.63 |
0.5568 | 293.15 | 859.691 |
0.5568 | 298.15 | 855.668 |
0.5568 | 303.15 | 851.665 |
0.5568 | 308.15 | 847.701 |
0.6107 | 288.15 | 872.206 |
0.6107 | 293.15 | 868.299 |
0.6107 | 298.15 | 864.217 |
0.6107 | 303.15 | 860.198 |
0.6107 | 308.15 | 856.228 |
0.6683 | 288.15 | 881.543 |
0.6683 | 293.15 | 877.641 |
0.6683 | 298.15 | 873.531 |
0.6683 | 303.15 | 869.475 |
0.6683 | 308.15 | 865.486 |
0.6924 | 288.15 | 885.505 |
0.6924 | 293.15 | 881.587 |
0.6924 | 298.15 | 877.468 |
0.6924 | 303.15 | 873.41 |
0.6924 | 308.15 | 869.396 |
0.7544 | 288.15 | 895.808 |
0.7544 | 293.15 | 891.893 |
0.7544 | 298.15 | 887.746 |
0.7544 | 303.15 | 883.674 |
0.7544 | 308.15 | 879.592 |
0.7963 | 288.15 | 902.873 |
0.7963 | 293.15 | 898.935 |
0.7963 | 298.15 | 894.791 |
0.7963 | 303.15 | 890.73 |
0.7963 | 308.15 | 886.574 |
0.8580 | 288.15 | 913.335 |
0.8580 | 293.15 | 909.366 |
0.8580 | 298.15 | 905.245 |
0.8580 | 303.15 | 901.206 |
0.8580 | 308.15 | 896.983 |
0.9079 | 288.15 | 921.784 |
0.9079 | 293.15 | 917.773 |
0.9079 | 298.15 | 913.7 |
0.9079 | 303.15 | 909.674 |
0.9079 | 308.15 | 905.434 |
0.9553 | 288.15 | 929.676 |
0.9553 | 293.15 | 925.674 |
0.9553 | 298.15 | 921.63 |
0.9553 | 303.15 | 917.622 |
0.9553 | 308.15 | 913.46 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
0.1168 | 288.15 | 1294.0 |
0.1168 | 293.15 | 1274.86 |
0.1168 | 298.15 | 1255.97 |
0.1168 | 303.15 | 1237.35 |
0.1168 | 308.15 | 1219.04 |
0.1659 | 288.15 | 1298.17 |
0.1659 | 293.15 | 1279.15 |
0.1659 | 298.15 | 1260.3 |
0.1659 | 303.15 | 1241.7 |
0.1659 | 308.15 | 1223.38 |
0.2092 | 288.15 | 1302.06 |
0.2092 | 293.15 | 1283.1 |
0.2092 | 298.15 | 1264.34 |
0.2092 | 303.15 | 1245.84 |
0.2092 | 308.15 | 1227.47 |
0.2589 | 288.15 | 1306.8 |
0.2589 | 293.15 | 1287.92 |
0.2589 | 298.15 | 1269.25 |
0.2589 | 303.15 | 1250.78 |
0.2589 | 308.15 | 1232.48 |
0.3155 | 288.15 | 1312.56 |
0.3155 | 293.15 | 1293.77 |
0.3155 | 298.15 | 1275.16 |
0.3155 | 303.15 | 1256.82 |
0.3155 | 308.15 | 1238.57 |
0.3564 | 288.15 | 1316.92 |
0.3564 | 293.15 | 1298.2 |
0.3564 | 298.15 | 1279.68 |
0.3564 | 303.15 | 1261.41 |
0.3564 | 308.15 | 1243.23 |
0.3830 | 288.15 | 1319.83 |
0.3830 | 293.15 | 1301.19 |
0.3830 | 298.15 | 1282.7 |
0.3830 | 303.15 | 1264.51 |
0.3830 | 308.15 | 1246.36 |
0.4544 | 288.15 | 1328.05 |
0.4544 | 293.15 | 1309.53 |
0.4544 | 298.15 | 1291.2 |
0.4544 | 303.15 | 1273.2 |
0.4544 | 308.15 | 1255.19 |
0.5108 | 288.15 | 1334.89 |
0.5108 | 293.15 | 1316.53 |
0.5108 | 298.15 | 1298.27 |
0.5108 | 303.15 | 1280.4 |
0.5108 | 308.15 | 1262.57 |
0.5568 | 288.15 | 1340.69 |
0.5568 | 293.15 | 1322.44 |
0.5568 | 298.15 | 1304.29 |
0.5568 | 303.15 | 1286.52 |
0.5568 | 308.15 | 1268.83 |
0.6107 | 288.15 | 1347.74 |
0.6107 | 293.15 | 1329.59 |
0.6107 | 298.15 | 1311.58 |
0.6107 | 303.15 | 1293.98 |
0.6107 | 308.15 | 1276.38 |
0.6683 | 288.15 | 1355.56 |
0.6683 | 293.15 | 1337.54 |
0.6683 | 298.15 | 1319.68 |
0.6683 | 303.15 | 1302.25 |
0.6683 | 308.15 | 1284.77 |
0.6924 | 288.15 | 1358.91 |
0.6924 | 293.15 | 1340.94 |
0.6924 | 298.15 | 1323.16 |
0.6924 | 303.15 | 1305.8 |
0.6924 | 308.15 | 1288.36 |
0.7544 | 288.15 | 1367.76 |
0.7544 | 293.15 | 1349.97 |
0.7544 | 298.15 | 1332.33 |
0.7544 | 303.15 | 1315.15 |
0.7544 | 308.15 | 1297.81 |
0.7963 | 288.15 | 1373.92 |
0.7963 | 293.15 | 1356.22 |
0.7963 | 298.15 | 1338.74 |
0.7963 | 303.15 | 1321.64 |
0.7963 | 308.15 | 1304.36 |
0.8580 | 288.15 | 1383.21 |
0.8580 | 293.15 | 1365.72 |
0.8580 | 298.15 | 1348.35 |
0.8580 | 303.15 | 1331.46 |
0.8580 | 308.15 | 1314.21 |
0.9079 | 288.15 | 1390.94 |
0.9079 | 293.15 | 1373.58 |
0.9079 | 298.15 | 1356.38 |
0.9079 | 303.15 | 1339.62 |
0.9079 | 308.15 | 1322.35 |
0.9553 | 288.15 | 1398.43 |
0.9553 | 293.15 | 1381.26 |
0.9553 | 298.15 | 1364.2 |
0.9553 | 303.15 | 1347.56 |
0.9553 | 308.15 | 1330.18 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
0.1168 | 288.15 | 1294.0 |
0.1168 | 293.15 | 1274.86 |
0.1168 | 298.15 | 1255.97 |
0.1168 | 303.15 | 1237.35 |
0.1168 | 308.15 | 1219.04 |
0.1659 | 288.15 | 1298.17 |
0.1659 | 293.15 | 1279.15 |
0.1659 | 298.15 | 1260.3 |
0.1659 | 303.15 | 1241.7 |
0.1659 | 308.15 | 1223.38 |
0.2092 | 288.15 | 1302.06 |
0.2092 | 293.15 | 1283.1 |
0.2092 | 298.15 | 1264.34 |
0.2092 | 303.15 | 1245.84 |
0.2092 | 308.15 | 1227.47 |
0.2589 | 288.15 | 1306.8 |
0.2589 | 293.15 | 1287.92 |
0.2589 | 298.15 | 1269.25 |
0.2589 | 303.15 | 1250.78 |
0.2589 | 308.15 | 1232.48 |
0.3155 | 288.15 | 1312.56 |
0.3155 | 293.15 | 1293.77 |
0.3155 | 298.15 | 1275.16 |
0.3155 | 303.15 | 1256.82 |
0.3155 | 308.15 | 1238.57 |
0.3564 | 288.15 | 1316.92 |
0.3564 | 293.15 | 1298.2 |
0.3564 | 298.15 | 1279.68 |
0.3564 | 303.15 | 1261.41 |
0.3564 | 308.15 | 1243.23 |
0.3830 | 288.15 | 1319.83 |
0.3830 | 293.15 | 1301.19 |
0.3830 | 298.15 | 1282.7 |
0.3830 | 303.15 | 1264.51 |
0.3830 | 308.15 | 1246.36 |
0.4544 | 288.15 | 1328.05 |
0.4544 | 293.15 | 1309.53 |
0.4544 | 298.15 | 1291.2 |
0.4544 | 303.15 | 1273.2 |
0.4544 | 308.15 | 1255.19 |
0.5108 | 288.15 | 1334.89 |
0.5108 | 293.15 | 1316.53 |
0.5108 | 298.15 | 1298.27 |
0.5108 | 303.15 | 1280.4 |
0.5108 | 308.15 | 1262.57 |
0.5568 | 288.15 | 1340.69 |
0.5568 | 293.15 | 1322.44 |
0.5568 | 298.15 | 1304.29 |
0.5568 | 303.15 | 1286.52 |
0.5568 | 308.15 | 1268.83 |
0.6107 | 288.15 | 1347.74 |
0.6107 | 293.15 | 1329.59 |
0.6107 | 298.15 | 1311.58 |
0.6107 | 303.15 | 1293.98 |
0.6107 | 308.15 | 1276.38 |
0.6683 | 288.15 | 1355.56 |
0.6683 | 293.15 | 1337.54 |
0.6683 | 298.15 | 1319.68 |
0.6683 | 303.15 | 1302.25 |
0.6683 | 308.15 | 1284.77 |
0.6924 | 288.15 | 1358.91 |
0.6924 | 293.15 | 1340.94 |
0.6924 | 298.15 | 1323.16 |
0.6924 | 303.15 | 1305.8 |
0.6924 | 308.15 | 1288.36 |
0.7544 | 288.15 | 1367.76 |
0.7544 | 293.15 | 1349.97 |
0.7544 | 298.15 | 1332.33 |
0.7544 | 303.15 | 1315.15 |
0.7544 | 308.15 | 1297.81 |
0.7963 | 288.15 | 1373.92 |
0.7963 | 293.15 | 1356.22 |
0.7963 | 298.15 | 1338.74 |
0.7963 | 303.15 | 1321.64 |
0.7963 | 308.15 | 1304.36 |
0.8580 | 288.15 | 1383.21 |
0.8580 | 293.15 | 1365.72 |
0.8580 | 298.15 | 1348.35 |
0.8580 | 303.15 | 1331.46 |
0.8580 | 308.15 | 1314.21 |
0.9079 | 288.15 | 1390.94 |
0.9079 | 293.15 | 1373.58 |
0.9079 | 298.15 | 1356.38 |
0.9079 | 303.15 | 1339.62 |
0.9079 | 308.15 | 1322.35 |
0.9553 | 288.15 | 1398.43 |
0.9553 | 293.15 | 1381.26 |
0.9553 | 298.15 | 1364.2 |
0.9553 | 303.15 | 1347.56 |
0.9553 | 308.15 | 1330.18 |