Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1165 | 853.467 |
| 288.15 | 0.1620 | 865.705 |
| 288.15 | 0.2113 | 875.875 |
| 288.15 | 0.2660 | 884.716 |
| 288.15 | 0.3119 | 890.88 |
| 288.15 | 0.3606 | 896.388 |
| 288.15 | 0.4012 | 900.31 |
| 288.15 | 0.4577 | 904.872 |
| 288.15 | 0.5071 | 908.159 |
| 288.15 | 0.5578 | 911.041 |
| 288.15 | 0.6037 | 913.218 |
| 288.15 | 0.6644 | 915.682 |
| 288.15 | 0.7102 | 917.283 |
| 288.15 | 0.7533 | 918.633 |
| 288.15 | 0.7928 | 919.837 |
| 288.15 | 0.8517 | 921.511 |
| 288.15 | 0.9000 | 922.714 |
| 288.15 | 0.9674 | 924.001 |
| 298.15 | 0.1165 | 844.018 |
| 298.15 | 0.1620 | 856.244 |
| 298.15 | 0.2113 | 866.451 |
| 298.15 | 0.2660 | 875.458 |
| 298.15 | 0.3119 | 881.656 |
| 298.15 | 0.3606 | 887.19 |
| 298.15 | 0.4012 | 891.16 |
| 298.15 | 0.4577 | 895.844 |
| 298.15 | 0.5071 | 899.262 |
| 298.15 | 0.5578 | 902.168 |
| 298.15 | 0.6037 | 904.353 |
| 298.15 | 0.6644 | 906.87 |
| 298.15 | 0.7102 | 908.456 |
| 298.15 | 0.7533 | 909.864 |
| 298.15 | 0.7928 | 911.054 |
| 298.15 | 0.8517 | 912.714 |
| 298.15 | 0.9000 | 913.911 |
| 298.15 | 0.9674 | 915.182 |
| 308.15 | 0.1165 | 834.816 |
| 308.15 | 0.1620 | 846.965 |
| 308.15 | 0.2113 | 857.177 |
| 308.15 | 0.2660 | 866.337 |
| 308.15 | 0.3119 | 872.742 |
| 308.15 | 0.3606 | 878.481 |
| 308.15 | 0.4012 | 882.585 |
| 308.15 | 0.4577 | 887.363 |
| 308.15 | 0.5071 | 890.741 |
| 308.15 | 0.5578 | 893.568 |
| 308.15 | 0.6037 | 895.701 |
| 308.15 | 0.6644 | 898.078 |
| 308.15 | 0.7102 | 899.602 |
| 308.15 | 0.7533 | 901.011 |
| 308.15 | 0.7928 | 902.199 |
| 308.15 | 0.8517 | 903.777 |
| 308.15 | 0.9000 | 905.244 |
| 308.15 | 0.9674 | 906.508 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1171 | 857.614 |
| 288.15 | 0.1668 | 872.157 |
| 288.15 | 0.2024 | 880.483 |
| 288.15 | 0.2453 | 888.765 |
| 288.15 | 0.3057 | 898.209 |
| 288.15 | 0.3572 | 904.718 |
| 288.15 | 0.4098 | 910.278 |
| 288.15 | 0.4448 | 913.47 |
| 288.15 | 0.4937 | 917.368 |
| 288.15 | 0.5565 | 921.596 |
| 288.15 | 0.6009 | 924.097 |
| 288.15 | 0.6571 | 926.86 |
| 288.15 | 0.7060 | 928.905 |
| 288.15 | 0.7491 | 930.523 |
| 288.15 | 0.8092 | 932.473 |
| 288.15 | 0.8524 | 933.727 |
| 288.15 | 0.9191 | 935.357 |
| 288.15 | 0.9648 | 936.301 |
| 293.15 | 0.1171 | 853.235 |
| 293.15 | 0.1668 | 867.848 |
| 293.15 | 0.2024 | 876.228 |
| 293.15 | 0.2453 | 884.567 |
| 293.15 | 0.3057 | 894.04 |
| 293.15 | 0.3572 | 900.582 |
| 293.15 | 0.4098 | 906.172 |
| 293.15 | 0.4448 | 909.378 |
| 293.15 | 0.4937 | 913.292 |
| 293.15 | 0.5565 | 917.544 |
| 293.15 | 0.6009 | 920.053 |
| 293.15 | 0.6571 | 922.837 |
| 293.15 | 0.7060 | 924.882 |
| 293.15 | 0.7491 | 926.512 |
| 293.15 | 0.8092 | 928.466 |
| 293.15 | 0.8524 | 929.728 |
| 293.15 | 0.9191 | 931.362 |
| 293.15 | 0.9648 | 932.315 |
| 298.15 | 0.1171 | 848.836 |
| 298.15 | 0.1668 | 863.53 |
| 298.15 | 0.2024 | 871.945 |
| 298.15 | 0.2453 | 880.311 |
| 298.15 | 0.3057 | 889.862 |
| 298.15 | 0.3572 | 896.438 |
| 298.15 | 0.4098 | 902.054 |
| 298.15 | 0.4448 | 905.279 |
| 298.15 | 0.4937 | 909.209 |
| 298.15 | 0.5565 | 913.483 |
| 298.15 | 0.6009 | 916.001 |
| 298.15 | 0.6571 | 918.802 |
| 298.15 | 0.7060 | 920.854 |
| 298.15 | 0.7491 | 922.492 |
| 298.15 | 0.8092 | 924.455 |
| 298.15 | 0.8524 | 925.721 |
| 298.15 | 0.9191 | 927.363 |
| 298.15 | 0.9648 | 928.32 |
| 303.15 | 0.1171 | 844.014 |
| 303.15 | 0.1668 | 858.918 |
| 303.15 | 0.2024 | 867.485 |
| 303.15 | 0.2453 | 876.022 |
| 303.15 | 0.3057 | 885.669 |
| 303.15 | 0.3572 | 892.28 |
| 303.15 | 0.4098 | 897.927 |
| 303.15 | 0.4448 | 901.168 |
| 303.15 | 0.4937 | 905.126 |
| 303.15 | 0.5565 | 909.382 |
| 303.15 | 0.6009 | 911.941 |
| 303.15 | 0.6571 | 914.739 |
| 303.15 | 0.7060 | 916.819 |
| 303.15 | 0.7491 | 918.464 |
| 303.15 | 0.8092 | 920.452 |
| 303.15 | 0.8524 | 921.707 |
| 303.15 | 0.9191 | 923.357 |
| 303.15 | 0.9648 | 924.323 |
| 308.15 | 0.1171 | 839.086 |
| 308.15 | 0.1668 | 854.278 |
| 308.15 | 0.2024 | 862.986 |
| 308.15 | 0.2453 | 871.662 |
| 308.15 | 0.3057 | 881.465 |
| 308.15 | 0.3572 | 888.145 |
| 308.15 | 0.4098 | 893.806 |
| 308.15 | 0.4448 | 897.051 |
| 308.15 | 0.4937 | 901.018 |
| 308.15 | 0.5565 | 905.302 |
| 308.15 | 0.6009 | 907.876 |
| 308.15 | 0.6571 | 910.687 |
| 308.15 | 0.7060 | 912.777 |
| 308.15 | 0.7491 | 914.429 |
| 308.15 | 0.8092 | 916.435 |
| 308.15 | 0.8524 | 917.689 |
| 308.15 | 0.9191 | 919.349 |
| 308.15 | 0.9648 | 920.308 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1165 | 853.467 |
| 288.15 | 0.1620 | 865.705 |
| 288.15 | 0.2113 | 875.875 |
| 288.15 | 0.2660 | 884.716 |
| 288.15 | 0.3119 | 890.88 |
| 288.15 | 0.3606 | 896.388 |
| 288.15 | 0.4012 | 900.31 |
| 288.15 | 0.4577 | 904.872 |
| 288.15 | 0.5071 | 908.159 |
| 288.15 | 0.5578 | 911.041 |
| 288.15 | 0.6037 | 913.218 |
| 288.15 | 0.6644 | 915.682 |
| 288.15 | 0.7102 | 917.283 |
| 288.15 | 0.7533 | 918.633 |
| 288.15 | 0.7928 | 919.837 |
| 288.15 | 0.8517 | 921.511 |
| 288.15 | 0.9000 | 922.714 |
| 288.15 | 0.9674 | 924.001 |
| 298.15 | 0.1165 | 844.018 |
| 298.15 | 0.1620 | 856.244 |
| 298.15 | 0.2113 | 866.451 |
| 298.15 | 0.2660 | 875.458 |
| 298.15 | 0.3119 | 881.656 |
| 298.15 | 0.3606 | 887.19 |
| 298.15 | 0.4012 | 891.16 |
| 298.15 | 0.4577 | 895.844 |
| 298.15 | 0.5071 | 899.262 |
| 298.15 | 0.5578 | 902.168 |
| 298.15 | 0.6037 | 904.353 |
| 298.15 | 0.6644 | 906.87 |
| 298.15 | 0.7102 | 908.456 |
| 298.15 | 0.7533 | 909.864 |
| 298.15 | 0.7928 | 911.054 |
| 298.15 | 0.8517 | 912.714 |
| 298.15 | 0.9000 | 913.911 |
| 298.15 | 0.9674 | 915.182 |
| 308.15 | 0.1165 | 834.816 |
| 308.15 | 0.1620 | 846.965 |
| 308.15 | 0.2113 | 857.177 |
| 308.15 | 0.2660 | 866.337 |
| 308.15 | 0.3119 | 872.742 |
| 308.15 | 0.3606 | 878.481 |
| 308.15 | 0.4012 | 882.585 |
| 308.15 | 0.4577 | 887.363 |
| 308.15 | 0.5071 | 890.741 |
| 308.15 | 0.5578 | 893.568 |
| 308.15 | 0.6037 | 895.701 |
| 308.15 | 0.6644 | 898.078 |
| 308.15 | 0.7102 | 899.602 |
| 308.15 | 0.7533 | 901.011 |
| 308.15 | 0.7928 | 902.199 |
| 308.15 | 0.8517 | 903.777 |
| 308.15 | 0.9000 | 905.244 |
| 308.15 | 0.9674 | 906.508 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1171 | 857.614 |
| 288.15 | 0.1668 | 872.157 |
| 288.15 | 0.2024 | 880.483 |
| 288.15 | 0.2453 | 888.765 |
| 288.15 | 0.3057 | 898.209 |
| 288.15 | 0.3572 | 904.718 |
| 288.15 | 0.4098 | 910.278 |
| 288.15 | 0.4448 | 913.47 |
| 288.15 | 0.4937 | 917.368 |
| 288.15 | 0.5565 | 921.596 |
| 288.15 | 0.6009 | 924.097 |
| 288.15 | 0.6571 | 926.86 |
| 288.15 | 0.7060 | 928.905 |
| 288.15 | 0.7491 | 930.523 |
| 288.15 | 0.8092 | 932.473 |
| 288.15 | 0.8524 | 933.727 |
| 288.15 | 0.9191 | 935.357 |
| 288.15 | 0.9648 | 936.301 |
| 293.15 | 0.1171 | 853.235 |
| 293.15 | 0.1668 | 867.848 |
| 293.15 | 0.2024 | 876.228 |
| 293.15 | 0.2453 | 884.567 |
| 293.15 | 0.3057 | 894.04 |
| 293.15 | 0.3572 | 900.582 |
| 293.15 | 0.4098 | 906.172 |
| 293.15 | 0.4448 | 909.378 |
| 293.15 | 0.4937 | 913.292 |
| 293.15 | 0.5565 | 917.544 |
| 293.15 | 0.6009 | 920.053 |
| 293.15 | 0.6571 | 922.837 |
| 293.15 | 0.7060 | 924.882 |
| 293.15 | 0.7491 | 926.512 |
| 293.15 | 0.8092 | 928.466 |
| 293.15 | 0.8524 | 929.728 |
| 293.15 | 0.9191 | 931.362 |
| 293.15 | 0.9648 | 932.315 |
| 298.15 | 0.1171 | 848.836 |
| 298.15 | 0.1668 | 863.53 |
| 298.15 | 0.2024 | 871.945 |
| 298.15 | 0.2453 | 880.311 |
| 298.15 | 0.3057 | 889.862 |
| 298.15 | 0.3572 | 896.438 |
| 298.15 | 0.4098 | 902.054 |
| 298.15 | 0.4448 | 905.279 |
| 298.15 | 0.4937 | 909.209 |
| 298.15 | 0.5565 | 913.483 |
| 298.15 | 0.6009 | 916.001 |
| 298.15 | 0.6571 | 918.802 |
| 298.15 | 0.7060 | 920.854 |
| 298.15 | 0.7491 | 922.492 |
| 298.15 | 0.8092 | 924.455 |
| 298.15 | 0.8524 | 925.721 |
| 298.15 | 0.9191 | 927.363 |
| 298.15 | 0.9648 | 928.32 |
| 303.15 | 0.1171 | 844.014 |
| 303.15 | 0.1668 | 858.918 |
| 303.15 | 0.2024 | 867.485 |
| 303.15 | 0.2453 | 876.022 |
| 303.15 | 0.3057 | 885.669 |
| 303.15 | 0.3572 | 892.28 |
| 303.15 | 0.4098 | 897.927 |
| 303.15 | 0.4448 | 901.168 |
| 303.15 | 0.4937 | 905.126 |
| 303.15 | 0.5565 | 909.382 |
| 303.15 | 0.6009 | 911.941 |
| 303.15 | 0.6571 | 914.739 |
| 303.15 | 0.7060 | 916.819 |
| 303.15 | 0.7491 | 918.464 |
| 303.15 | 0.8092 | 920.452 |
| 303.15 | 0.8524 | 921.707 |
| 303.15 | 0.9191 | 923.357 |
| 303.15 | 0.9648 | 924.323 |
| 308.15 | 0.1171 | 839.086 |
| 308.15 | 0.1668 | 854.278 |
| 308.15 | 0.2024 | 862.986 |
| 308.15 | 0.2453 | 871.662 |
| 308.15 | 0.3057 | 881.465 |
| 308.15 | 0.3572 | 888.145 |
| 308.15 | 0.4098 | 893.806 |
| 308.15 | 0.4448 | 897.051 |
| 308.15 | 0.4937 | 901.018 |
| 308.15 | 0.5565 | 905.302 |
| 308.15 | 0.6009 | 907.876 |
| 308.15 | 0.6571 | 910.687 |
| 308.15 | 0.7060 | 912.777 |
| 308.15 | 0.7491 | 914.429 |
| 308.15 | 0.8092 | 916.435 |
| 308.15 | 0.8524 | 917.689 |
| 308.15 | 0.9191 | 919.349 |
| 308.15 | 0.9648 | 920.308 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 0.1171 | 288.15 | 1247.43 |
| 0.1171 | 293.15 | 1230.88 |
| 0.1171 | 298.15 | 1214.37 |
| 0.1171 | 303.15 | 1197.93 |
| 0.1171 | 308.15 | 1181.59 |
| 0.1668 | 288.15 | 1271.08 |
| 0.1668 | 293.15 | 1254.37 |
| 0.1668 | 298.15 | 1237.92 |
| 0.1668 | 303.15 | 1221.4 |
| 0.1668 | 308.15 | 1205.14 |
| 0.2024 | 288.15 | 1286.22 |
| 0.2024 | 293.15 | 1269.52 |
| 0.2024 | 298.15 | 1252.93 |
| 0.2024 | 303.15 | 1236.5 |
| 0.2024 | 308.15 | 1220.2 |
| 0.2453 | 288.15 | 1302.64 |
| 0.2453 | 293.15 | 1285.94 |
| 0.2453 | 298.15 | 1269.34 |
| 0.2453 | 303.15 | 1252.85 |
| 0.2453 | 308.15 | 1236.48 |
| 0.3057 | 288.15 | 1322.67 |
| 0.3057 | 293.15 | 1305.85 |
| 0.3057 | 298.15 | 1289.23 |
| 0.3057 | 303.15 | 1272.7 |
| 0.3057 | 308.15 | 1256.33 |
| 0.3572 | 288.15 | 1336.96 |
| 0.3572 | 293.15 | 1320.15 |
| 0.3572 | 298.15 | 1303.54 |
| 0.3572 | 303.15 | 1286.97 |
| 0.3572 | 308.15 | 1270.44 |
| 0.4098 | 288.15 | 1349.38 |
| 0.4098 | 293.15 | 1332.52 |
| 0.4098 | 298.15 | 1315.94 |
| 0.4098 | 303.15 | 1299.34 |
| 0.4098 | 308.15 | 1282.77 |
| 0.4448 | 288.15 | 1356.47 |
| 0.4448 | 293.15 | 1339.58 |
| 0.4448 | 298.15 | 1322.95 |
| 0.4448 | 303.15 | 1306.3 |
| 0.4448 | 308.15 | 1289.79 |
| 0.4937 | 288.15 | 1365.04 |
| 0.4937 | 293.15 | 1348.23 |
| 0.4937 | 298.15 | 1331.49 |
| 0.4937 | 303.15 | 1314.77 |
| 0.4937 | 308.15 | 1298.23 |
| 0.5565 | 288.15 | 1373.9 |
| 0.5565 | 293.15 | 1357.1 |
| 0.5565 | 298.15 | 1340.3 |
| 0.5565 | 303.15 | 1323.6 |
| 0.5565 | 308.15 | 1307.0 |
| 0.6009 | 288.15 | 1379.12 |
| 0.6009 | 293.15 | 1362.26 |
| 0.6009 | 298.15 | 1345.46 |
| 0.6009 | 303.15 | 1328.67 |
| 0.6009 | 308.15 | 1312.04 |
| 0.6571 | 288.15 | 1384.47 |
| 0.6571 | 293.15 | 1367.62 |
| 0.6571 | 298.15 | 1350.76 |
| 0.6571 | 303.15 | 1333.94 |
| 0.6571 | 308.15 | 1317.36 |
| 0.7060 | 288.15 | 1388.34 |
| 0.7060 | 293.15 | 1371.42 |
| 0.7060 | 298.15 | 1354.54 |
| 0.7060 | 303.15 | 1337.74 |
| 0.7060 | 308.15 | 1320.99 |
| 0.7491 | 288.15 | 1391.28 |
| 0.7491 | 293.15 | 1374.35 |
| 0.7491 | 298.15 | 1357.47 |
| 0.7491 | 303.15 | 1340.61 |
| 0.7491 | 308.15 | 1323.85 |
| 0.8092 | 288.15 | 1394.9 |
| 0.8092 | 293.15 | 1377.98 |
| 0.8092 | 298.15 | 1360.98 |
| 0.8092 | 303.15 | 1344.23 |
| 0.8092 | 308.15 | 1327.48 |
| 0.8524 | 288.15 | 1397.34 |
| 0.8524 | 293.15 | 1380.37 |
| 0.8524 | 298.15 | 1363.41 |
| 0.8524 | 303.15 | 1346.61 |
| 0.8524 | 308.15 | 1329.87 |
| 0.9191 | 288.15 | 1401.3 |
| 0.9191 | 293.15 | 1384.21 |
| 0.9191 | 298.15 | 1367.24 |
| 0.9191 | 303.15 | 1350.43 |
| 0.9191 | 308.15 | 1333.75 |
| 0.9648 | 288.15 | 1404.14 |
| 0.9648 | 293.15 | 1387.05 |
| 0.9648 | 298.15 | 1370.05 |
| 0.9648 | 303.15 | 1353.33 |
| 0.9648 | 308.15 | 1336.67 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Diethylene glycol hexyl ether (1) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 0.1171 | 288.15 | 1247.43 |
| 0.1171 | 293.15 | 1230.88 |
| 0.1171 | 298.15 | 1214.37 |
| 0.1171 | 303.15 | 1197.93 |
| 0.1171 | 308.15 | 1181.59 |
| 0.1668 | 288.15 | 1271.08 |
| 0.1668 | 293.15 | 1254.37 |
| 0.1668 | 298.15 | 1237.92 |
| 0.1668 | 303.15 | 1221.4 |
| 0.1668 | 308.15 | 1205.14 |
| 0.2024 | 288.15 | 1286.22 |
| 0.2024 | 293.15 | 1269.52 |
| 0.2024 | 298.15 | 1252.93 |
| 0.2024 | 303.15 | 1236.5 |
| 0.2024 | 308.15 | 1220.2 |
| 0.2453 | 288.15 | 1302.64 |
| 0.2453 | 293.15 | 1285.94 |
| 0.2453 | 298.15 | 1269.34 |
| 0.2453 | 303.15 | 1252.85 |
| 0.2453 | 308.15 | 1236.48 |
| 0.3057 | 288.15 | 1322.67 |
| 0.3057 | 293.15 | 1305.85 |
| 0.3057 | 298.15 | 1289.23 |
| 0.3057 | 303.15 | 1272.7 |
| 0.3057 | 308.15 | 1256.33 |
| 0.3572 | 288.15 | 1336.96 |
| 0.3572 | 293.15 | 1320.15 |
| 0.3572 | 298.15 | 1303.54 |
| 0.3572 | 303.15 | 1286.97 |
| 0.3572 | 308.15 | 1270.44 |
| 0.4098 | 288.15 | 1349.38 |
| 0.4098 | 293.15 | 1332.52 |
| 0.4098 | 298.15 | 1315.94 |
| 0.4098 | 303.15 | 1299.34 |
| 0.4098 | 308.15 | 1282.77 |
| 0.4448 | 288.15 | 1356.47 |
| 0.4448 | 293.15 | 1339.58 |
| 0.4448 | 298.15 | 1322.95 |
| 0.4448 | 303.15 | 1306.3 |
| 0.4448 | 308.15 | 1289.79 |
| 0.4937 | 288.15 | 1365.04 |
| 0.4937 | 293.15 | 1348.23 |
| 0.4937 | 298.15 | 1331.49 |
| 0.4937 | 303.15 | 1314.77 |
| 0.4937 | 308.15 | 1298.23 |
| 0.5565 | 288.15 | 1373.9 |
| 0.5565 | 293.15 | 1357.1 |
| 0.5565 | 298.15 | 1340.3 |
| 0.5565 | 303.15 | 1323.6 |
| 0.5565 | 308.15 | 1307.0 |
| 0.6009 | 288.15 | 1379.12 |
| 0.6009 | 293.15 | 1362.26 |
| 0.6009 | 298.15 | 1345.46 |
| 0.6009 | 303.15 | 1328.67 |
| 0.6009 | 308.15 | 1312.04 |
| 0.6571 | 288.15 | 1384.47 |
| 0.6571 | 293.15 | 1367.62 |
| 0.6571 | 298.15 | 1350.76 |
| 0.6571 | 303.15 | 1333.94 |
| 0.6571 | 308.15 | 1317.36 |
| 0.7060 | 288.15 | 1388.34 |
| 0.7060 | 293.15 | 1371.42 |
| 0.7060 | 298.15 | 1354.54 |
| 0.7060 | 303.15 | 1337.74 |
| 0.7060 | 308.15 | 1320.99 |
| 0.7491 | 288.15 | 1391.28 |
| 0.7491 | 293.15 | 1374.35 |
| 0.7491 | 298.15 | 1357.47 |
| 0.7491 | 303.15 | 1340.61 |
| 0.7491 | 308.15 | 1323.85 |
| 0.8092 | 288.15 | 1394.9 |
| 0.8092 | 293.15 | 1377.98 |
| 0.8092 | 298.15 | 1360.98 |
| 0.8092 | 303.15 | 1344.23 |
| 0.8092 | 308.15 | 1327.48 |
| 0.8524 | 288.15 | 1397.34 |
| 0.8524 | 293.15 | 1380.37 |
| 0.8524 | 298.15 | 1363.41 |
| 0.8524 | 303.15 | 1346.61 |
| 0.8524 | 308.15 | 1329.87 |
| 0.9191 | 288.15 | 1401.3 |
| 0.9191 | 293.15 | 1384.21 |
| 0.9191 | 298.15 | 1367.24 |
| 0.9191 | 303.15 | 1350.43 |
| 0.9191 | 308.15 | 1333.75 |
| 0.9648 | 288.15 | 1404.14 |
| 0.9648 | 293.15 | 1387.05 |
| 0.9648 | 298.15 | 1370.05 |
| 0.9648 | 303.15 | 1353.33 |
| 0.9648 | 308.15 | 1336.67 |