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 |
0.1165 | 288.15 | 788.964 |
0.1165 | 293.15 | 784.34 |
0.1165 | 298.15 | 779.774 |
0.1165 | 303.15 | 775.186 |
0.1165 | 308.15 | 770.602 |
0.1587 | 288.15 | 803.568 |
0.1587 | 293.15 | 799.044 |
0.1587 | 298.15 | 794.52 |
0.1587 | 303.15 | 790.0 |
0.1587 | 308.15 | 785.486 |
0.1943 | 288.15 | 814.988 |
0.1943 | 293.15 | 810.552 |
0.1943 | 298.15 | 806.078 |
0.1943 | 303.15 | 801.606 |
0.1943 | 308.15 | 797.118 |
0.2403 | 288.15 | 828.571 |
0.2403 | 293.15 | 824.179 |
0.2403 | 298.15 | 819.765 |
0.2403 | 303.15 | 815.333 |
0.2403 | 308.15 | 810.88 |
0.2974 | 288.15 | 843.631 |
0.2974 | 293.15 | 839.297 |
0.2974 | 298.15 | 834.939 |
0.2974 | 303.15 | 830.566 |
0.2974 | 308.15 | 826.173 |
0.3403 | 288.15 | 853.769 |
0.3403 | 293.15 | 849.458 |
0.3403 | 298.15 | 845.129 |
0.3403 | 303.15 | 840.783 |
0.3403 | 308.15 | 836.421 |
0.3916 | 288.15 | 864.666 |
0.3916 | 293.15 | 860.386 |
0.3916 | 298.15 | 856.092 |
0.3916 | 303.15 | 851.78 |
0.3916 | 308.15 | 847.457 |
0.4568 | 288.15 | 876.866 |
0.4568 | 293.15 | 872.668 |
0.4568 | 298.15 | 868.407 |
0.4568 | 303.15 | 864.132 |
0.4568 | 308.15 | 859.843 |
0.5105 | 288.15 | 885.772 |
0.5105 | 293.15 | 881.607 |
0.5105 | 298.15 | 877.388 |
0.5105 | 303.15 | 873.158 |
0.5105 | 308.15 | 868.903 |
0.5658 | 288.15 | 894.125 |
0.5658 | 293.15 | 889.991 |
0.5658 | 298.15 | 885.768 |
0.5658 | 303.15 | 881.571 |
0.5658 | 308.15 | 877.355 |
0.6081 | 288.15 | 900.031 |
0.6081 | 293.15 | 895.896 |
0.6081 | 298.15 | 891.728 |
0.6081 | 303.15 | 887.547 |
0.6081 | 308.15 | 883.355 |
0.6559 | 288.15 | 906.287 |
0.6559 | 293.15 | 902.162 |
0.6559 | 298.15 | 898.025 |
0.6559 | 303.15 | 893.876 |
0.6559 | 308.15 | 889.716 |
0.6977 | 288.15 | 911.396 |
0.6977 | 293.15 | 907.303 |
0.6977 | 298.15 | 903.194 |
0.6977 | 303.15 | 899.074 |
0.6977 | 308.15 | 894.942 |
0.7402 | 288.15 | 916.322 |
0.7402 | 293.15 | 912.248 |
0.7402 | 298.15 | 908.162 |
0.7402 | 303.15 | 904.067 |
0.7402 | 308.15 | 899.964 |
0.8029 | 288.15 | 923.0 |
0.8029 | 293.15 | 918.949 |
0.8029 | 298.15 | 914.893 |
0.8029 | 303.15 | 910.805 |
0.8029 | 308.15 | 906.755 |
0.8675 | 288.15 | 928.954 |
0.8675 | 293.15 | 924.929 |
0.8675 | 298.15 | 920.91 |
0.8675 | 303.15 | 916.89 |
0.8675 | 308.15 | 912.833 |
0.9082 | 288.15 | 932.126 |
0.9082 | 293.15 | 928.121 |
0.9082 | 298.15 | 924.113 |
0.9082 | 303.15 | 920.095 |
0.9082 | 308.15 | 916.07 |
0.9635 | 288.15 | 935.472 |
0.9635 | 293.15 | 931.477 |
0.9635 | 298.15 | 927.494 |
0.9635 | 303.15 | 923.492 |
0.9635 | 308.15 | 919.484 |
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 |
0.1165 | 288.15 | 788.964 |
0.1165 | 293.15 | 784.34 |
0.1165 | 298.15 | 779.774 |
0.1165 | 303.15 | 775.186 |
0.1165 | 308.15 | 770.602 |
0.1587 | 288.15 | 803.568 |
0.1587 | 293.15 | 799.044 |
0.1587 | 298.15 | 794.52 |
0.1587 | 303.15 | 790.0 |
0.1587 | 308.15 | 785.486 |
0.1943 | 288.15 | 814.988 |
0.1943 | 293.15 | 810.552 |
0.1943 | 298.15 | 806.078 |
0.1943 | 303.15 | 801.606 |
0.1943 | 308.15 | 797.118 |
0.2403 | 288.15 | 828.571 |
0.2403 | 293.15 | 824.179 |
0.2403 | 298.15 | 819.765 |
0.2403 | 303.15 | 815.333 |
0.2403 | 308.15 | 810.88 |
0.2974 | 288.15 | 843.631 |
0.2974 | 293.15 | 839.297 |
0.2974 | 298.15 | 834.939 |
0.2974 | 303.15 | 830.566 |
0.2974 | 308.15 | 826.173 |
0.3403 | 288.15 | 853.769 |
0.3403 | 293.15 | 849.458 |
0.3403 | 298.15 | 845.129 |
0.3403 | 303.15 | 840.783 |
0.3403 | 308.15 | 836.421 |
0.3916 | 288.15 | 864.666 |
0.3916 | 293.15 | 860.386 |
0.3916 | 298.15 | 856.092 |
0.3916 | 303.15 | 851.78 |
0.3916 | 308.15 | 847.457 |
0.4568 | 288.15 | 876.866 |
0.4568 | 293.15 | 872.668 |
0.4568 | 298.15 | 868.407 |
0.4568 | 303.15 | 864.132 |
0.4568 | 308.15 | 859.843 |
0.5105 | 288.15 | 885.772 |
0.5105 | 293.15 | 881.607 |
0.5105 | 298.15 | 877.388 |
0.5105 | 303.15 | 873.158 |
0.5105 | 308.15 | 868.903 |
0.5658 | 288.15 | 894.125 |
0.5658 | 293.15 | 889.991 |
0.5658 | 298.15 | 885.768 |
0.5658 | 303.15 | 881.571 |
0.5658 | 308.15 | 877.355 |
0.6081 | 288.15 | 900.031 |
0.6081 | 293.15 | 895.896 |
0.6081 | 298.15 | 891.728 |
0.6081 | 303.15 | 887.547 |
0.6081 | 308.15 | 883.355 |
0.6559 | 288.15 | 906.287 |
0.6559 | 293.15 | 902.162 |
0.6559 | 298.15 | 898.025 |
0.6559 | 303.15 | 893.876 |
0.6559 | 308.15 | 889.716 |
0.6977 | 288.15 | 911.396 |
0.6977 | 293.15 | 907.303 |
0.6977 | 298.15 | 903.194 |
0.6977 | 303.15 | 899.074 |
0.6977 | 308.15 | 894.942 |
0.7402 | 288.15 | 916.322 |
0.7402 | 293.15 | 912.248 |
0.7402 | 298.15 | 908.162 |
0.7402 | 303.15 | 904.067 |
0.7402 | 308.15 | 899.964 |
0.8029 | 288.15 | 923.0 |
0.8029 | 293.15 | 918.949 |
0.8029 | 298.15 | 914.893 |
0.8029 | 303.15 | 910.805 |
0.8029 | 308.15 | 906.755 |
0.8675 | 288.15 | 928.954 |
0.8675 | 293.15 | 924.929 |
0.8675 | 298.15 | 920.91 |
0.8675 | 303.15 | 916.89 |
0.8675 | 308.15 | 912.833 |
0.9082 | 288.15 | 932.126 |
0.9082 | 293.15 | 928.121 |
0.9082 | 298.15 | 924.113 |
0.9082 | 303.15 | 920.095 |
0.9082 | 308.15 | 916.07 |
0.9635 | 288.15 | 935.472 |
0.9635 | 293.15 | 931.477 |
0.9635 | 298.15 | 927.494 |
0.9635 | 303.15 | 923.492 |
0.9635 | 308.15 | 919.484 |
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 |
0.1165 | 288.15 | 1322.97 |
0.1165 | 293.15 | 1302.22 |
0.1165 | 298.15 | 1281.5 |
0.1165 | 303.15 | 1260.84 |
0.1165 | 308.15 | 1240.34 |
0.1587 | 288.15 | 1332.27 |
0.1587 | 293.15 | 1311.99 |
0.1587 | 298.15 | 1291.67 |
0.1587 | 303.15 | 1271.49 |
0.1587 | 308.15 | 1251.29 |
0.1943 | 288.15 | 1339.54 |
0.1943 | 293.15 | 1319.68 |
0.1943 | 298.15 | 1299.68 |
0.1943 | 303.15 | 1279.79 |
0.1943 | 308.15 | 1259.85 |
0.2403 | 288.15 | 1348.18 |
0.2403 | 293.15 | 1328.73 |
0.2403 | 298.15 | 1309.11 |
0.2403 | 303.15 | 1289.63 |
0.2403 | 308.15 | 1270.0 |
0.2974 | 288.15 | 1357.78 |
0.2974 | 293.15 | 1338.75 |
0.2974 | 298.15 | 1319.61 |
0.2974 | 303.15 | 1300.56 |
0.2974 | 308.15 | 1281.34 |
0.3403 | 288.15 | 1364.21 |
0.3403 | 293.15 | 1345.54 |
0.3403 | 298.15 | 1326.64 |
0.3403 | 303.15 | 1307.87 |
0.3403 | 308.15 | 1288.93 |
0.3916 | 288.15 | 1371.09 |
0.3916 | 293.15 | 1352.63 |
0.3916 | 298.15 | 1334.08 |
0.3916 | 303.15 | 1315.65 |
0.3916 | 308.15 | 1297.07 |
0.4568 | 288.15 | 1378.62 |
0.4568 | 293.15 | 1360.44 |
0.4568 | 298.15 | 1342.25 |
0.4568 | 303.15 | 1324.16 |
0.4568 | 308.15 | 1306.0 |
0.5105 | 288.15 | 1383.9 |
0.5105 | 293.15 | 1365.88 |
0.5105 | 298.15 | 1348.0 |
0.5105 | 303.15 | 1330.09 |
0.5105 | 308.15 | 1312.26 |
0.5658 | 288.15 | 1388.52 |
0.5658 | 293.15 | 1370.68 |
0.5658 | 298.15 | 1353.01 |
0.5658 | 303.15 | 1335.29 |
0.5658 | 308.15 | 1317.75 |
0.6081 | 288.15 | 1391.55 |
0.6081 | 293.15 | 1373.87 |
0.6081 | 298.15 | 1356.27 |
0.6081 | 303.15 | 1338.75 |
0.6081 | 308.15 | 1321.25 |
0.6559 | 288.15 | 1394.49 |
0.6559 | 293.15 | 1376.94 |
0.6559 | 298.15 | 1359.49 |
0.6559 | 303.15 | 1342.08 |
0.6559 | 308.15 | 1324.9 |
0.6977 | 288.15 | 1396.68 |
0.6977 | 293.15 | 1379.21 |
0.6977 | 298.15 | 1361.85 |
0.6977 | 303.15 | 1344.55 |
0.6977 | 308.15 | 1327.53 |
0.7402 | 288.15 | 1398.57 |
0.7402 | 293.15 | 1381.2 |
0.7402 | 298.15 | 1363.91 |
0.7402 | 303.15 | 1346.71 |
0.7402 | 308.15 | 1329.8 |
0.8029 | 288.15 | 1400.81 |
0.8029 | 293.15 | 1383.52 |
0.8029 | 298.15 | 1366.38 |
0.8029 | 303.15 | 1349.31 |
0.8029 | 308.15 | 1332.55 |
0.8675 | 288.15 | 1402.53 |
0.8675 | 293.15 | 1385.39 |
0.8675 | 298.15 | 1368.32 |
0.8675 | 303.15 | 1351.36 |
0.8675 | 308.15 | 1334.62 |
0.9082 | 288.15 | 1403.37 |
0.9082 | 293.15 | 1386.3 |
0.9082 | 298.15 | 1369.33 |
0.9082 | 303.15 | 1352.42 |
0.9082 | 308.15 | 1335.69 |
0.9635 | 288.15 | 1404.26 |
0.9635 | 293.15 | 1387.36 |
0.9635 | 298.15 | 1370.39 |
0.9635 | 303.15 | 1353.58 |
0.9635 | 308.15 | 1336.81 |
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 |
0.1165 | 288.15 | 1322.97 |
0.1165 | 293.15 | 1302.22 |
0.1165 | 298.15 | 1281.5 |
0.1165 | 303.15 | 1260.84 |
0.1165 | 308.15 | 1240.34 |
0.1587 | 288.15 | 1332.27 |
0.1587 | 293.15 | 1311.99 |
0.1587 | 298.15 | 1291.67 |
0.1587 | 303.15 | 1271.49 |
0.1587 | 308.15 | 1251.29 |
0.1943 | 288.15 | 1339.54 |
0.1943 | 293.15 | 1319.68 |
0.1943 | 298.15 | 1299.68 |
0.1943 | 303.15 | 1279.79 |
0.1943 | 308.15 | 1259.85 |
0.2403 | 288.15 | 1348.18 |
0.2403 | 293.15 | 1328.73 |
0.2403 | 298.15 | 1309.11 |
0.2403 | 303.15 | 1289.63 |
0.2403 | 308.15 | 1270.0 |
0.2974 | 288.15 | 1357.78 |
0.2974 | 293.15 | 1338.75 |
0.2974 | 298.15 | 1319.61 |
0.2974 | 303.15 | 1300.56 |
0.2974 | 308.15 | 1281.34 |
0.3403 | 288.15 | 1364.21 |
0.3403 | 293.15 | 1345.54 |
0.3403 | 298.15 | 1326.64 |
0.3403 | 303.15 | 1307.87 |
0.3403 | 308.15 | 1288.93 |
0.3916 | 288.15 | 1371.09 |
0.3916 | 293.15 | 1352.63 |
0.3916 | 298.15 | 1334.08 |
0.3916 | 303.15 | 1315.65 |
0.3916 | 308.15 | 1297.07 |
0.4568 | 288.15 | 1378.62 |
0.4568 | 293.15 | 1360.44 |
0.4568 | 298.15 | 1342.25 |
0.4568 | 303.15 | 1324.16 |
0.4568 | 308.15 | 1306.0 |
0.5105 | 288.15 | 1383.9 |
0.5105 | 293.15 | 1365.88 |
0.5105 | 298.15 | 1348.0 |
0.5105 | 303.15 | 1330.09 |
0.5105 | 308.15 | 1312.26 |
0.5658 | 288.15 | 1388.52 |
0.5658 | 293.15 | 1370.68 |
0.5658 | 298.15 | 1353.01 |
0.5658 | 303.15 | 1335.29 |
0.5658 | 308.15 | 1317.75 |
0.6081 | 288.15 | 1391.55 |
0.6081 | 293.15 | 1373.87 |
0.6081 | 298.15 | 1356.27 |
0.6081 | 303.15 | 1338.75 |
0.6081 | 308.15 | 1321.25 |
0.6559 | 288.15 | 1394.49 |
0.6559 | 293.15 | 1376.94 |
0.6559 | 298.15 | 1359.49 |
0.6559 | 303.15 | 1342.08 |
0.6559 | 308.15 | 1324.9 |
0.6977 | 288.15 | 1396.68 |
0.6977 | 293.15 | 1379.21 |
0.6977 | 298.15 | 1361.85 |
0.6977 | 303.15 | 1344.55 |
0.6977 | 308.15 | 1327.53 |
0.7402 | 288.15 | 1398.57 |
0.7402 | 293.15 | 1381.2 |
0.7402 | 298.15 | 1363.91 |
0.7402 | 303.15 | 1346.71 |
0.7402 | 308.15 | 1329.8 |
0.8029 | 288.15 | 1400.81 |
0.8029 | 293.15 | 1383.52 |
0.8029 | 298.15 | 1366.38 |
0.8029 | 303.15 | 1349.31 |
0.8029 | 308.15 | 1332.55 |
0.8675 | 288.15 | 1402.53 |
0.8675 | 293.15 | 1385.39 |
0.8675 | 298.15 | 1368.32 |
0.8675 | 303.15 | 1351.36 |
0.8675 | 308.15 | 1334.62 |
0.9082 | 288.15 | 1403.37 |
0.9082 | 293.15 | 1386.3 |
0.9082 | 298.15 | 1369.33 |
0.9082 | 303.15 | 1352.42 |
0.9082 | 308.15 | 1335.69 |
0.9635 | 288.15 | 1404.26 |
0.9635 | 293.15 | 1387.36 |
0.9635 | 298.15 | 1370.39 |
0.9635 | 303.15 | 1353.58 |
0.9635 | 308.15 | 1336.81 |