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 | 0.1197 | 844.686 |
| 288.15 | 0.1597 | 850.265 |
| 288.15 | 0.2026 | 856.07 |
| 288.15 | 0.2644 | 864.155 |
| 288.15 | 0.3070 | 869.559 |
| 288.15 | 0.3555 | 875.557 |
| 288.15 | 0.4163 | 882.781 |
| 288.15 | 0.4444 | 886.01 |
| 288.15 | 0.4965 | 891.772 |
| 288.15 | 0.5490 | 897.332 |
| 288.15 | 0.6118 | 903.667 |
| 288.15 | 0.6743 | 909.713 |
| 288.15 | 0.7680 | 918.369 |
| 288.15 | 0.8158 | 922.63 |
| 288.15 | 0.8551 | 926.049 |
| 288.15 | 0.8989 | 929.693 |
| 288.15 | 0.9536 | 933.886 |
| 293.15 | 0.1197 | 841.1 |
| 293.15 | 0.1597 | 846.652 |
| 293.15 | 0.2026 | 852.422 |
| 293.15 | 0.2644 | 860.487 |
| 293.15 | 0.3070 | 865.861 |
| 293.15 | 0.3555 | 871.836 |
| 293.15 | 0.4163 | 879.042 |
| 293.15 | 0.4444 | 882.239 |
| 293.15 | 0.4965 | 888.0 |
| 293.15 | 0.5490 | 893.538 |
| 293.15 | 0.6118 | 899.843 |
| 293.15 | 0.6743 | 905.849 |
| 293.15 | 0.7680 | 914.461 |
| 293.15 | 0.8158 | 918.71 |
| 293.15 | 0.8551 | 922.107 |
| 293.15 | 0.8989 | 925.738 |
| 293.15 | 0.9536 | 929.912 |
| 298.15 | 0.1197 | 837.482 |
| 298.15 | 0.1597 | 843.022 |
| 298.15 | 0.2026 | 848.773 |
| 298.15 | 0.2644 | 856.802 |
| 298.15 | 0.3070 | 862.153 |
| 298.15 | 0.3555 | 868.101 |
| 298.15 | 0.4163 | 875.254 |
| 298.15 | 0.4444 | 878.454 |
| 298.15 | 0.4965 | 884.176 |
| 298.15 | 0.5490 | 889.686 |
| 298.15 | 0.6118 | 895.968 |
| 298.15 | 0.6743 | 901.96 |
| 298.15 | 0.7680 | 910.543 |
| 298.15 | 0.8158 | 914.779 |
| 298.15 | 0.8551 | 918.16 |
| 298.15 | 0.8989 | 921.775 |
| 298.15 | 0.9536 | 925.937 |
| 303.15 | 0.1197 | 833.883 |
| 303.15 | 0.1597 | 839.38 |
| 303.15 | 0.2026 | 845.1 |
| 303.15 | 0.2644 | 853.102 |
| 303.15 | 0.3070 | 858.429 |
| 303.15 | 0.3555 | 864.353 |
| 303.15 | 0.4163 | 871.484 |
| 303.15 | 0.4444 | 874.673 |
| 303.15 | 0.4965 | 880.358 |
| 303.15 | 0.5490 | 885.851 |
| 303.15 | 0.6118 | 892.105 |
| 303.15 | 0.6743 | 898.071 |
| 303.15 | 0.7680 | 906.62 |
| 303.15 | 0.8158 | 910.838 |
| 303.15 | 0.8551 | 914.207 |
| 303.15 | 0.8989 | 917.818 |
| 303.15 | 0.9536 | 921.952 |
| 308.15 | 0.1197 | 830.252 |
| 308.15 | 0.1597 | 835.719 |
| 308.15 | 0.2026 | 841.399 |
| 308.15 | 0.2644 | 849.355 |
| 308.15 | 0.3070 | 854.692 |
| 308.15 | 0.3555 | 860.592 |
| 308.15 | 0.4163 | 867.685 |
| 308.15 | 0.4444 | 870.856 |
| 308.15 | 0.4965 | 876.528 |
| 308.15 | 0.5490 | 882.0 |
| 308.15 | 0.6118 | 888.229 |
| 308.15 | 0.6743 | 894.164 |
| 308.15 | 0.7680 | 902.693 |
| 308.15 | 0.8158 | 906.89 |
| 308.15 | 0.8551 | 910.251 |
| 308.15 | 0.8989 | 913.838 |
| 308.15 | 0.9536 | 917.965 |
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 | 0.1109 | 840.489 |
| 288.15 | 0.1592 | 846.447 |
| 288.15 | 0.1986 | 851.154 |
| 288.15 | 0.2580 | 857.994 |
| 288.15 | 0.3094 | 863.644 |
| 288.15 | 0.3515 | 868.149 |
| 288.15 | 0.3927 | 872.418 |
| 288.15 | 0.4463 | 877.834 |
| 288.15 | 0.5084 | 883.872 |
| 288.15 | 0.5574 | 888.492 |
| 288.15 | 0.6167 | 893.921 |
| 288.15 | 0.6511 | 896.97 |
| 288.15 | 0.7101 | 902.042 |
| 288.15 | 0.7491 | 905.269 |
| 288.15 | 0.8085 | 910.029 |
| 288.15 | 0.8543 | 913.588 |
| 288.15 | 0.9087 | 917.663 |
| 288.15 | 0.9487 | 920.583 |
| 298.15 | 0.1109 | 833.182 |
| 298.15 | 0.1592 | 839.091 |
| 298.15 | 0.1986 | 843.756 |
| 298.15 | 0.2580 | 850.491 |
| 298.15 | 0.3094 | 856.08 |
| 298.15 | 0.3515 | 860.468 |
| 298.15 | 0.3927 | 864.636 |
| 298.15 | 0.4463 | 869.912 |
| 298.15 | 0.5084 | 875.796 |
| 298.15 | 0.5574 | 880.349 |
| 298.15 | 0.6167 | 885.645 |
| 298.15 | 0.6511 | 888.674 |
| 298.15 | 0.7101 | 893.703 |
| 298.15 | 0.7491 | 896.923 |
| 298.15 | 0.8085 | 901.658 |
| 298.15 | 0.8543 | 905.198 |
| 298.15 | 0.9087 | 909.197 |
| 298.15 | 0.9487 | 912.028 |
| 308.15 | 0.1109 | 825.922 |
| 308.15 | 0.1592 | 831.645 |
| 308.15 | 0.1986 | 836.178 |
| 308.15 | 0.2580 | 842.797 |
| 308.15 | 0.3094 | 848.254 |
| 308.15 | 0.3515 | 852.588 |
| 308.15 | 0.3927 | 856.716 |
| 308.15 | 0.4463 | 861.89 |
| 308.15 | 0.5084 | 867.692 |
| 308.15 | 0.5574 | 872.159 |
| 308.15 | 0.6167 | 877.389 |
| 308.15 | 0.6511 | 880.331 |
| 308.15 | 0.7101 | 885.279 |
| 308.15 | 0.7491 | 888.446 |
| 308.15 | 0.8085 | 893.122 |
| 308.15 | 0.8543 | 896.613 |
| 308.15 | 0.9087 | 900.531 |
| 308.15 | 0.9487 | 903.307 |
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 | 0.1197 | 1367.47 |
| 288.15 | 0.1597 | 1369.55 |
| 288.15 | 0.2026 | 1371.68 |
| 288.15 | 0.2644 | 1374.54 |
| 288.15 | 0.3070 | 1376.56 |
| 288.15 | 0.3555 | 1378.78 |
| 288.15 | 0.4163 | 1381.63 |
| 288.15 | 0.4444 | 1382.72 |
| 288.15 | 0.4965 | 1385.16 |
| 288.15 | 0.5490 | 1387.38 |
| 288.15 | 0.6118 | 1389.96 |
| 288.15 | 0.6743 | 1392.56 |
| 288.15 | 0.7680 | 1396.3 |
| 288.15 | 0.8158 | 1398.17 |
| 288.15 | 0.8551 | 1399.72 |
| 288.15 | 0.8989 | 1401.42 |
| 288.15 | 0.9536 | 1403.55 |
| 293.15 | 0.1197 | 1350.47 |
| 293.15 | 0.1597 | 1352.58 |
| 293.15 | 0.2026 | 1354.72 |
| 293.15 | 0.2644 | 1357.65 |
| 293.15 | 0.3070 | 1359.64 |
| 293.15 | 0.3555 | 1361.92 |
| 293.15 | 0.4163 | 1364.66 |
| 293.15 | 0.4444 | 1365.92 |
| 293.15 | 0.4965 | 1368.22 |
| 293.15 | 0.5490 | 1370.51 |
| 293.15 | 0.6118 | 1373.15 |
| 293.15 | 0.6743 | 1375.8 |
| 293.15 | 0.7680 | 1379.5 |
| 293.15 | 0.8158 | 1381.31 |
| 293.15 | 0.8551 | 1382.82 |
| 293.15 | 0.8989 | 1384.47 |
| 293.15 | 0.9536 | 1386.53 |
| 298.15 | 0.1197 | 1333.57 |
| 298.15 | 0.1597 | 1335.65 |
| 298.15 | 0.2026 | 1337.77 |
| 298.15 | 0.2644 | 1340.83 |
| 298.15 | 0.3070 | 1342.74 |
| 298.15 | 0.3555 | 1345.09 |
| 298.15 | 0.4163 | 1347.81 |
| 298.15 | 0.4444 | 1349.16 |
| 298.15 | 0.4965 | 1351.46 |
| 298.15 | 0.5490 | 1353.67 |
| 298.15 | 0.6118 | 1356.41 |
| 298.15 | 0.6743 | 1359.02 |
| 298.15 | 0.7680 | 1362.68 |
| 298.15 | 0.8158 | 1364.44 |
| 298.15 | 0.8551 | 1365.98 |
| 298.15 | 0.8989 | 1367.53 |
| 298.15 | 0.9536 | 1369.58 |
| 303.15 | 0.1197 | 1316.83 |
| 303.15 | 0.1597 | 1318.94 |
| 303.15 | 0.2026 | 1321.03 |
| 303.15 | 0.2644 | 1324.06 |
| 303.15 | 0.3070 | 1326.05 |
| 303.15 | 0.3555 | 1328.34 |
| 303.15 | 0.4163 | 1331.13 |
| 303.15 | 0.4444 | 1332.28 |
| 303.15 | 0.4965 | 1334.7 |
| 303.15 | 0.5490 | 1336.92 |
| 303.15 | 0.6118 | 1339.56 |
| 303.15 | 0.6743 | 1342.08 |
| 303.15 | 0.7680 | 1345.82 |
| 303.15 | 0.8158 | 1347.61 |
| 303.15 | 0.8551 | 1349.12 |
| 303.15 | 0.8989 | 1350.83 |
| 303.15 | 0.9536 | 1352.8 |
| 308.15 | 0.1197 | 1300.23 |
| 308.15 | 0.1597 | 1302.33 |
| 308.15 | 0.2026 | 1304.48 |
| 308.15 | 0.2644 | 1307.41 |
| 308.15 | 0.3070 | 1309.51 |
| 308.15 | 0.3555 | 1311.69 |
| 308.15 | 0.4163 | 1314.58 |
| 308.15 | 0.4444 | 1315.74 |
| 308.15 | 0.4965 | 1318.12 |
| 308.15 | 0.5490 | 1320.26 |
| 308.15 | 0.6118 | 1323.02 |
| 308.15 | 0.6743 | 1325.52 |
| 308.15 | 0.7680 | 1329.24 |
| 308.15 | 0.8158 | 1330.97 |
| 308.15 | 0.8551 | 1332.49 |
| 308.15 | 0.8989 | 1334.06 |
| 308.15 | 0.9536 | 1336.14 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.