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 | 0.1112 | 837.545 |
288.15 | 0.1587 | 846.35 |
288.15 | 0.2096 | 855.128 |
288.15 | 0.2584 | 862.625 |
288.15 | 0.3012 | 868.44 |
288.15 | 0.3558 | 874.88 |
288.15 | 0.4022 | 879.672 |
288.15 | 0.4506 | 884.17 |
288.15 | 0.5069 | 889.049 |
288.15 | 0.5410 | 891.897 |
288.15 | 0.5971 | 896.445 |
288.15 | 0.6456 | 900.337 |
288.15 | 0.6998 | 904.59 |
288.15 | 0.7470 | 908.177 |
288.15 | 0.8052 | 912.354 |
288.15 | 0.8501 | 915.348 |
288.15 | 0.9008 | 918.511 |
288.15 | 0.9459 | 921.161 |
298.15 | 0.1112 | 830.059 |
298.15 | 0.1587 | 838.122 |
298.15 | 0.2096 | 846.145 |
298.15 | 0.2584 | 853.171 |
298.15 | 0.3012 | 858.72 |
298.15 | 0.3558 | 865.166 |
298.15 | 0.4022 | 870.098 |
298.15 | 0.4506 | 874.849 |
298.15 | 0.5069 | 880.057 |
298.15 | 0.5410 | 883.079 |
298.15 | 0.5971 | 887.853 |
298.15 | 0.6456 | 891.848 |
298.15 | 0.6998 | 896.131 |
298.15 | 0.7470 | 899.702 |
298.15 | 0.8052 | 903.888 |
298.15 | 0.8501 | 906.892 |
298.15 | 0.9008 | 910.007 |
298.15 | 0.9459 | 912.609 |
308.15 | 0.1112 | 822.319 |
308.15 | 0.1587 | 830.389 |
308.15 | 0.2096 | 838.566 |
308.15 | 0.2584 | 845.659 |
308.15 | 0.3012 | 851.35 |
308.15 | 0.3558 | 857.77 |
308.15 | 0.4022 | 862.642 |
308.15 | 0.4506 | 867.245 |
308.15 | 0.5069 | 872.125 |
308.15 | 0.5410 | 874.951 |
308.15 | 0.5971 | 879.382 |
308.15 | 0.6456 | 883.098 |
308.15 | 0.6998 | 887.198 |
308.15 | 0.7470 | 890.721 |
308.15 | 0.8052 | 894.96 |
308.15 | 0.8501 | 898.056 |
308.15 | 0.9008 | 901.375 |
308.15 | 0.9459 | 903.991 |
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 | 0.1078 | 841.1 |
288.15 | 0.1622 | 850.687 |
288.15 | 0.2069 | 858.039 |
288.15 | 0.2553 | 865.554 |
288.15 | 0.2980 | 871.838 |
288.15 | 0.3646 | 880.994 |
288.15 | 0.4027 | 885.886 |
288.15 | 0.4509 | 891.699 |
288.15 | 0.4972 | 896.896 |
288.15 | 0.5422 | 901.582 |
288.15 | 0.6161 | 908.619 |
288.15 | 0.6680 | 913.212 |
288.15 | 0.6985 | 915.788 |
288.15 | 0.7544 | 920.338 |
288.15 | 0.8055 | 924.361 |
288.15 | 0.8476 | 927.543 |
288.15 | 0.8950 | 930.931 |
288.15 | 0.9529 | 934.588 |
293.15 | 0.1078 | 837.386 |
293.15 | 0.1622 | 846.94 |
293.15 | 0.2069 | 854.267 |
293.15 | 0.2553 | 861.758 |
293.15 | 0.2980 | 868.024 |
293.15 | 0.3646 | 877.155 |
293.15 | 0.4027 | 882.034 |
293.15 | 0.4509 | 887.834 |
293.15 | 0.4972 | 892.991 |
293.15 | 0.5422 | 897.684 |
293.15 | 0.6161 | 904.704 |
293.15 | 0.6680 | 909.288 |
293.15 | 0.6985 | 911.857 |
293.15 | 0.7544 | 916.395 |
293.15 | 0.8055 | 920.411 |
293.15 | 0.8476 | 923.58 |
293.15 | 0.8950 | 926.961 |
293.15 | 0.9529 | 930.609 |
298.15 | 0.1078 | 833.637 |
298.15 | 0.1622 | 843.17 |
298.15 | 0.2069 | 850.477 |
298.15 | 0.2553 | 857.946 |
298.15 | 0.2980 | 864.196 |
298.15 | 0.3646 | 873.301 |
298.15 | 0.4027 | 878.17 |
298.15 | 0.4509 | 883.952 |
298.15 | 0.4972 | 889.123 |
298.15 | 0.5422 | 893.794 |
298.15 | 0.6161 | 900.801 |
298.15 | 0.6680 | 905.354 |
298.15 | 0.6985 | 907.915 |
298.15 | 0.7544 | 912.444 |
298.15 | 0.8055 | 916.444 |
298.15 | 0.8476 | 919.614 |
298.15 | 0.8950 | 922.988 |
298.15 | 0.9529 | 926.624 |
303.15 | 0.1078 | 829.874 |
303.15 | 0.1622 | 839.38 |
303.15 | 0.2069 | 846.668 |
303.15 | 0.2553 | 854.12 |
303.15 | 0.2980 | 860.35 |
303.15 | 0.3646 | 869.461 |
303.15 | 0.4027 | 874.29 |
303.15 | 0.4509 | 880.058 |
303.15 | 0.4972 | 885.216 |
303.15 | 0.5422 | 889.855 |
303.15 | 0.6161 | 896.846 |
303.15 | 0.6680 | 901.411 |
303.15 | 0.6985 | 903.967 |
303.15 | 0.7544 | 908.482 |
303.15 | 0.8055 | 912.476 |
303.15 | 0.8476 | 915.638 |
303.15 | 0.8950 | 919.003 |
303.15 | 0.9529 | 922.635 |
308.15 | 0.1078 | 825.998 |
308.15 | 0.1622 | 835.531 |
308.15 | 0.2069 | 842.838 |
308.15 | 0.2553 | 850.275 |
308.15 | 0.2980 | 856.491 |
308.15 | 0.3646 | 865.566 |
308.15 | 0.4027 | 870.397 |
308.15 | 0.4509 | 876.149 |
308.15 | 0.4972 | 881.265 |
308.15 | 0.5422 | 885.892 |
308.15 | 0.6161 | 892.904 |
308.15 | 0.6680 | 897.456 |
308.15 | 0.6985 | 900.011 |
308.15 | 0.7544 | 904.53 |
308.15 | 0.8055 | 908.502 |
308.15 | 0.8476 | 911.655 |
308.15 | 0.8950 | 915.012 |
308.15 | 0.9529 | 918.64 |
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 | 0.1112 | 837.545 |
288.15 | 0.1587 | 846.35 |
288.15 | 0.2096 | 855.128 |
288.15 | 0.2584 | 862.625 |
288.15 | 0.3012 | 868.44 |
288.15 | 0.3558 | 874.88 |
288.15 | 0.4022 | 879.672 |
288.15 | 0.4506 | 884.17 |
288.15 | 0.5069 | 889.049 |
288.15 | 0.5410 | 891.897 |
288.15 | 0.5971 | 896.445 |
288.15 | 0.6456 | 900.337 |
288.15 | 0.6998 | 904.59 |
288.15 | 0.7470 | 908.177 |
288.15 | 0.8052 | 912.354 |
288.15 | 0.8501 | 915.348 |
288.15 | 0.9008 | 918.511 |
288.15 | 0.9459 | 921.161 |
298.15 | 0.1112 | 830.059 |
298.15 | 0.1587 | 838.122 |
298.15 | 0.2096 | 846.145 |
298.15 | 0.2584 | 853.171 |
298.15 | 0.3012 | 858.72 |
298.15 | 0.3558 | 865.166 |
298.15 | 0.4022 | 870.098 |
298.15 | 0.4506 | 874.849 |
298.15 | 0.5069 | 880.057 |
298.15 | 0.5410 | 883.079 |
298.15 | 0.5971 | 887.853 |
298.15 | 0.6456 | 891.848 |
298.15 | 0.6998 | 896.131 |
298.15 | 0.7470 | 899.702 |
298.15 | 0.8052 | 903.888 |
298.15 | 0.8501 | 906.892 |
298.15 | 0.9008 | 910.007 |
298.15 | 0.9459 | 912.609 |
308.15 | 0.1112 | 822.319 |
308.15 | 0.1587 | 830.389 |
308.15 | 0.2096 | 838.566 |
308.15 | 0.2584 | 845.659 |
308.15 | 0.3012 | 851.35 |
308.15 | 0.3558 | 857.77 |
308.15 | 0.4022 | 862.642 |
308.15 | 0.4506 | 867.245 |
308.15 | 0.5069 | 872.125 |
308.15 | 0.5410 | 874.951 |
308.15 | 0.5971 | 879.382 |
308.15 | 0.6456 | 883.098 |
308.15 | 0.6998 | 887.198 |
308.15 | 0.7470 | 890.721 |
308.15 | 0.8052 | 894.96 |
308.15 | 0.8501 | 898.056 |
308.15 | 0.9008 | 901.375 |
308.15 | 0.9459 | 903.991 |
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 | 0.1078 | 841.1 |
288.15 | 0.1622 | 850.687 |
288.15 | 0.2069 | 858.039 |
288.15 | 0.2553 | 865.554 |
288.15 | 0.2980 | 871.838 |
288.15 | 0.3646 | 880.994 |
288.15 | 0.4027 | 885.886 |
288.15 | 0.4509 | 891.699 |
288.15 | 0.4972 | 896.896 |
288.15 | 0.5422 | 901.582 |
288.15 | 0.6161 | 908.619 |
288.15 | 0.6680 | 913.212 |
288.15 | 0.6985 | 915.788 |
288.15 | 0.7544 | 920.338 |
288.15 | 0.8055 | 924.361 |
288.15 | 0.8476 | 927.543 |
288.15 | 0.8950 | 930.931 |
288.15 | 0.9529 | 934.588 |
293.15 | 0.1078 | 837.386 |
293.15 | 0.1622 | 846.94 |
293.15 | 0.2069 | 854.267 |
293.15 | 0.2553 | 861.758 |
293.15 | 0.2980 | 868.024 |
293.15 | 0.3646 | 877.155 |
293.15 | 0.4027 | 882.034 |
293.15 | 0.4509 | 887.834 |
293.15 | 0.4972 | 892.991 |
293.15 | 0.5422 | 897.684 |
293.15 | 0.6161 | 904.704 |
293.15 | 0.6680 | 909.288 |
293.15 | 0.6985 | 911.857 |
293.15 | 0.7544 | 916.395 |
293.15 | 0.8055 | 920.411 |
293.15 | 0.8476 | 923.58 |
293.15 | 0.8950 | 926.961 |
293.15 | 0.9529 | 930.609 |
298.15 | 0.1078 | 833.637 |
298.15 | 0.1622 | 843.17 |
298.15 | 0.2069 | 850.477 |
298.15 | 0.2553 | 857.946 |
298.15 | 0.2980 | 864.196 |
298.15 | 0.3646 | 873.301 |
298.15 | 0.4027 | 878.17 |
298.15 | 0.4509 | 883.952 |
298.15 | 0.4972 | 889.123 |
298.15 | 0.5422 | 893.794 |
298.15 | 0.6161 | 900.801 |
298.15 | 0.6680 | 905.354 |
298.15 | 0.6985 | 907.915 |
298.15 | 0.7544 | 912.444 |
298.15 | 0.8055 | 916.444 |
298.15 | 0.8476 | 919.614 |
298.15 | 0.8950 | 922.988 |
298.15 | 0.9529 | 926.624 |
303.15 | 0.1078 | 829.874 |
303.15 | 0.1622 | 839.38 |
303.15 | 0.2069 | 846.668 |
303.15 | 0.2553 | 854.12 |
303.15 | 0.2980 | 860.35 |
303.15 | 0.3646 | 869.461 |
303.15 | 0.4027 | 874.29 |
303.15 | 0.4509 | 880.058 |
303.15 | 0.4972 | 885.216 |
303.15 | 0.5422 | 889.855 |
303.15 | 0.6161 | 896.846 |
303.15 | 0.6680 | 901.411 |
303.15 | 0.6985 | 903.967 |
303.15 | 0.7544 | 908.482 |
303.15 | 0.8055 | 912.476 |
303.15 | 0.8476 | 915.638 |
303.15 | 0.8950 | 919.003 |
303.15 | 0.9529 | 922.635 |
308.15 | 0.1078 | 825.998 |
308.15 | 0.1622 | 835.531 |
308.15 | 0.2069 | 842.838 |
308.15 | 0.2553 | 850.275 |
308.15 | 0.2980 | 856.491 |
308.15 | 0.3646 | 865.566 |
308.15 | 0.4027 | 870.397 |
308.15 | 0.4509 | 876.149 |
308.15 | 0.4972 | 881.265 |
308.15 | 0.5422 | 885.892 |
308.15 | 0.6161 | 892.904 |
308.15 | 0.6680 | 897.456 |
308.15 | 0.6985 | 900.011 |
308.15 | 0.7544 | 904.53 |
308.15 | 0.8055 | 908.502 |
308.15 | 0.8476 | 911.655 |
308.15 | 0.8950 | 915.012 |
308.15 | 0.9529 | 918.64 |
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 | 0.1078 | 1327.31 |
288.15 | 0.1622 | 1335.1 |
288.15 | 0.2069 | 1341.08 |
288.15 | 0.2553 | 1347.1 |
288.15 | 0.2980 | 1352.12 |
288.15 | 0.3646 | 1359.43 |
288.15 | 0.4027 | 1363.3 |
288.15 | 0.4509 | 1367.87 |
288.15 | 0.4972 | 1372.1 |
288.15 | 0.5422 | 1375.93 |
288.15 | 0.6161 | 1381.7 |
288.15 | 0.6680 | 1385.46 |
288.15 | 0.6985 | 1387.59 |
288.15 | 0.7544 | 1391.33 |
288.15 | 0.8055 | 1394.44 |
288.15 | 0.8476 | 1396.98 |
288.15 | 0.8950 | 1399.8 |
288.15 | 0.9529 | 1402.94 |
293.15 | 0.1078 | 1310.31 |
293.15 | 0.1622 | 1318.16 |
293.15 | 0.2069 | 1324.1 |
293.15 | 0.2553 | 1330.13 |
293.15 | 0.2980 | 1335.19 |
293.15 | 0.3646 | 1342.5 |
293.15 | 0.4027 | 1346.33 |
293.15 | 0.4509 | 1351.05 |
293.15 | 0.4972 | 1355.15 |
293.15 | 0.5422 | 1359.0 |
293.15 | 0.6161 | 1364.7 |
293.15 | 0.6680 | 1368.57 |
293.15 | 0.6985 | 1370.58 |
293.15 | 0.7544 | 1374.3 |
293.15 | 0.8055 | 1377.49 |
293.15 | 0.8476 | 1379.92 |
293.15 | 0.8950 | 1382.7 |
293.15 | 0.9529 | 1385.88 |
298.15 | 0.1078 | 1293.5 |
298.15 | 0.1622 | 1301.3 |
298.15 | 0.2069 | 1307.29 |
298.15 | 0.2553 | 1313.31 |
298.15 | 0.2980 | 1318.33 |
298.15 | 0.3646 | 1325.75 |
298.15 | 0.4027 | 1329.57 |
298.15 | 0.4509 | 1334.24 |
298.15 | 0.4972 | 1338.46 |
298.15 | 0.5422 | 1342.3 |
298.15 | 0.6161 | 1347.91 |
298.15 | 0.6680 | 1351.73 |
298.15 | 0.6985 | 1353.78 |
298.15 | 0.7544 | 1357.5 |
298.15 | 0.8055 | 1360.51 |
298.15 | 0.8476 | 1363.0 |
298.15 | 0.8950 | 1365.86 |
298.15 | 0.9529 | 1368.92 |
303.15 | 0.1078 | 1276.85 |
303.15 | 0.1622 | 1284.68 |
303.15 | 0.2069 | 1290.6 |
303.15 | 0.2553 | 1296.61 |
303.15 | 0.2980 | 1301.64 |
303.15 | 0.3646 | 1308.99 |
303.15 | 0.4027 | 1312.79 |
303.15 | 0.4509 | 1317.5 |
303.15 | 0.4972 | 1321.6 |
303.15 | 0.5422 | 1325.38 |
303.15 | 0.6161 | 1331.11 |
303.15 | 0.6680 | 1334.94 |
303.15 | 0.6985 | 1336.97 |
303.15 | 0.7544 | 1340.65 |
303.15 | 0.8055 | 1343.76 |
303.15 | 0.8476 | 1346.23 |
303.15 | 0.8950 | 1349.0 |
303.15 | 0.9529 | 1352.15 |
308.15 | 0.1078 | 1260.15 |
308.15 | 0.1622 | 1268.0 |
308.15 | 0.2069 | 1274.01 |
308.15 | 0.2553 | 1280.02 |
308.15 | 0.2980 | 1285.16 |
308.15 | 0.3646 | 1292.44 |
308.15 | 0.4027 | 1296.22 |
308.15 | 0.4509 | 1300.91 |
308.15 | 0.4972 | 1305.06 |
308.15 | 0.5422 | 1308.81 |
308.15 | 0.6161 | 1314.54 |
308.15 | 0.6680 | 1318.25 |
308.15 | 0.6985 | 1320.38 |
308.15 | 0.7544 | 1324.02 |
308.15 | 0.8055 | 1327.13 |
308.15 | 0.8476 | 1329.65 |
308.15 | 0.8950 | 1332.32 |
308.15 | 0.9529 | 1335.47 |
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 | 0.1078 | 1327.31 |
288.15 | 0.1622 | 1335.1 |
288.15 | 0.2069 | 1341.08 |
288.15 | 0.2553 | 1347.1 |
288.15 | 0.2980 | 1352.12 |
288.15 | 0.3646 | 1359.43 |
288.15 | 0.4027 | 1363.3 |
288.15 | 0.4509 | 1367.87 |
288.15 | 0.4972 | 1372.1 |
288.15 | 0.5422 | 1375.93 |
288.15 | 0.6161 | 1381.7 |
288.15 | 0.6680 | 1385.46 |
288.15 | 0.6985 | 1387.59 |
288.15 | 0.7544 | 1391.33 |
288.15 | 0.8055 | 1394.44 |
288.15 | 0.8476 | 1396.98 |
288.15 | 0.8950 | 1399.8 |
288.15 | 0.9529 | 1402.94 |
293.15 | 0.1078 | 1310.31 |
293.15 | 0.1622 | 1318.16 |
293.15 | 0.2069 | 1324.1 |
293.15 | 0.2553 | 1330.13 |
293.15 | 0.2980 | 1335.19 |
293.15 | 0.3646 | 1342.5 |
293.15 | 0.4027 | 1346.33 |
293.15 | 0.4509 | 1351.05 |
293.15 | 0.4972 | 1355.15 |
293.15 | 0.5422 | 1359.0 |
293.15 | 0.6161 | 1364.7 |
293.15 | 0.6680 | 1368.57 |
293.15 | 0.6985 | 1370.58 |
293.15 | 0.7544 | 1374.3 |
293.15 | 0.8055 | 1377.49 |
293.15 | 0.8476 | 1379.92 |
293.15 | 0.8950 | 1382.7 |
293.15 | 0.9529 | 1385.88 |
298.15 | 0.1078 | 1293.5 |
298.15 | 0.1622 | 1301.3 |
298.15 | 0.2069 | 1307.29 |
298.15 | 0.2553 | 1313.31 |
298.15 | 0.2980 | 1318.33 |
298.15 | 0.3646 | 1325.75 |
298.15 | 0.4027 | 1329.57 |
298.15 | 0.4509 | 1334.24 |
298.15 | 0.4972 | 1338.46 |
298.15 | 0.5422 | 1342.3 |
298.15 | 0.6161 | 1347.91 |
298.15 | 0.6680 | 1351.73 |
298.15 | 0.6985 | 1353.78 |
298.15 | 0.7544 | 1357.5 |
298.15 | 0.8055 | 1360.51 |
298.15 | 0.8476 | 1363.0 |
298.15 | 0.8950 | 1365.86 |
298.15 | 0.9529 | 1368.92 |
303.15 | 0.1078 | 1276.85 |
303.15 | 0.1622 | 1284.68 |
303.15 | 0.2069 | 1290.6 |
303.15 | 0.2553 | 1296.61 |
303.15 | 0.2980 | 1301.64 |
303.15 | 0.3646 | 1308.99 |
303.15 | 0.4027 | 1312.79 |
303.15 | 0.4509 | 1317.5 |
303.15 | 0.4972 | 1321.6 |
303.15 | 0.5422 | 1325.38 |
303.15 | 0.6161 | 1331.11 |
303.15 | 0.6680 | 1334.94 |
303.15 | 0.6985 | 1336.97 |
303.15 | 0.7544 | 1340.65 |
303.15 | 0.8055 | 1343.76 |
303.15 | 0.8476 | 1346.23 |
303.15 | 0.8950 | 1349.0 |
303.15 | 0.9529 | 1352.15 |
308.15 | 0.1078 | 1260.15 |
308.15 | 0.1622 | 1268.0 |
308.15 | 0.2069 | 1274.01 |
308.15 | 0.2553 | 1280.02 |
308.15 | 0.2980 | 1285.16 |
308.15 | 0.3646 | 1292.44 |
308.15 | 0.4027 | 1296.22 |
308.15 | 0.4509 | 1300.91 |
308.15 | 0.4972 | 1305.06 |
308.15 | 0.5422 | 1308.81 |
308.15 | 0.6161 | 1314.54 |
308.15 | 0.6680 | 1318.25 |
308.15 | 0.6985 | 1320.38 |
308.15 | 0.7544 | 1324.02 |
308.15 | 0.8055 | 1327.13 |
308.15 | 0.8476 | 1329.65 |
308.15 | 0.8950 | 1332.32 |
308.15 | 0.9529 | 1335.47 |