Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0465 | 0.0021 |
| 298.15 | 0.1495 | 0.0029 |
| 298.15 | 0.2501 | 0.0040 |
| 298.15 | 0.3505 | 0.0055 |
| 298.15 | 0.4432 | 0.0072 |
| 298.15 | 0.4957 | 0.0084 |
| 298.15 | 0.5486 | 0.0099 |
| 298.15 | 0.6486 | 0.0132 |
| 298.15 | 0.7501 | 0.0175 |
| 298.15 | 0.8489 | 0.0230 |
| 298.15 | 0.9400 | 0.0294 |
| 308.15 | 0.0465 | 0.0018 |
| 308.15 | 0.1495 | 0.0023 |
| 308.15 | 0.2501 | 0.0031 |
| 308.15 | 0.3505 | 0.0040 |
| 308.15 | 0.4432 | 0.0052 |
| 308.15 | 0.4957 | 0.0060 |
| 308.15 | 0.5486 | 0.0068 |
| 308.15 | 0.6486 | 0.0089 |
| 308.15 | 0.7501 | 0.0115 |
| 308.15 | 0.8489 | 0.0147 |
| 308.15 | 0.9400 | 0.0184 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0465 | 0.0021 |
| 298.15 | 0.1495 | 0.0029 |
| 298.15 | 0.2501 | 0.0040 |
| 298.15 | 0.3505 | 0.0055 |
| 298.15 | 0.4432 | 0.0072 |
| 298.15 | 0.4957 | 0.0084 |
| 298.15 | 0.5486 | 0.0099 |
| 298.15 | 0.6486 | 0.0132 |
| 298.15 | 0.7501 | 0.0175 |
| 298.15 | 0.8489 | 0.0230 |
| 298.15 | 0.9400 | 0.0294 |
| 308.15 | 0.0465 | 0.0018 |
| 308.15 | 0.1495 | 0.0023 |
| 308.15 | 0.2501 | 0.0031 |
| 308.15 | 0.3505 | 0.0040 |
| 308.15 | 0.4432 | 0.0052 |
| 308.15 | 0.4957 | 0.0060 |
| 308.15 | 0.5486 | 0.0068 |
| 308.15 | 0.6486 | 0.0089 |
| 308.15 | 0.7501 | 0.0115 |
| 308.15 | 0.8489 | 0.0147 |
| 308.15 | 0.9400 | 0.0184 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0465 | 1193.04 |
| 298.15 | 0.1495 | 1181.96 |
| 298.15 | 0.2501 | 1171.96 |
| 298.15 | 0.3505 | 1162.79 |
| 298.15 | 0.4432 | 1155.0 |
| 298.15 | 0.4957 | 1150.86 |
| 298.15 | 0.5486 | 1146.89 |
| 298.15 | 0.6486 | 1139.88 |
| 298.15 | 0.7501 | 1133.38 |
| 298.15 | 0.8489 | 1127.59 |
| 298.15 | 0.9400 | 1122.66 |
| 303.15 | 0.0465 | 1188.21 |
| 303.15 | 0.1495 | 1177.18 |
| 303.15 | 0.2501 | 1167.27 |
| 303.15 | 0.3505 | 1158.19 |
| 303.15 | 0.4432 | 1150.5 |
| 303.15 | 0.4957 | 1146.43 |
| 303.15 | 0.5486 | 1142.52 |
| 303.15 | 0.6486 | 1135.64 |
| 303.15 | 0.7501 | 1129.28 |
| 303.15 | 0.8489 | 1123.64 |
| 303.15 | 0.9400 | 1118.85 |
| 308.15 | 0.0465 | 1182.99 |
| 308.15 | 0.1495 | 1172.05 |
| 308.15 | 0.2501 | 1162.24 |
| 308.15 | 0.3505 | 1153.27 |
| 308.15 | 0.4432 | 1145.7 |
| 308.15 | 0.4957 | 1141.69 |
| 308.15 | 0.5486 | 1137.86 |
| 308.15 | 0.6486 | 1131.12 |
| 308.15 | 0.7501 | 1124.93 |
| 308.15 | 0.8489 | 1119.45 |
| 308.15 | 0.9400 | 1114.82 |
| 313.15 | 0.0465 | 1178.15 |
| 313.15 | 0.1495 | 1167.49 |
| 313.15 | 0.2501 | 1157.93 |
| 313.15 | 0.3505 | 1149.22 |
| 313.15 | 0.4432 | 1141.87 |
| 313.15 | 0.4957 | 1138.0 |
| 313.15 | 0.5486 | 1134.3 |
| 313.15 | 0.6486 | 1127.81 |
| 313.15 | 0.7501 | 1121.87 |
| 313.15 | 0.8489 | 1116.64 |
| 313.15 | 0.9400 | 1112.24 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0465 | 1193.04 |
| 298.15 | 0.1495 | 1181.96 |
| 298.15 | 0.2501 | 1171.96 |
| 298.15 | 0.3505 | 1162.79 |
| 298.15 | 0.4432 | 1155.0 |
| 298.15 | 0.4957 | 1150.86 |
| 298.15 | 0.5486 | 1146.89 |
| 298.15 | 0.6486 | 1139.88 |
| 298.15 | 0.7501 | 1133.38 |
| 298.15 | 0.8489 | 1127.59 |
| 298.15 | 0.9400 | 1122.66 |
| 303.15 | 0.0465 | 1188.21 |
| 303.15 | 0.1495 | 1177.18 |
| 303.15 | 0.2501 | 1167.27 |
| 303.15 | 0.3505 | 1158.19 |
| 303.15 | 0.4432 | 1150.5 |
| 303.15 | 0.4957 | 1146.43 |
| 303.15 | 0.5486 | 1142.52 |
| 303.15 | 0.6486 | 1135.64 |
| 303.15 | 0.7501 | 1129.28 |
| 303.15 | 0.8489 | 1123.64 |
| 303.15 | 0.9400 | 1118.85 |
| 308.15 | 0.0465 | 1182.99 |
| 308.15 | 0.1495 | 1172.05 |
| 308.15 | 0.2501 | 1162.24 |
| 308.15 | 0.3505 | 1153.27 |
| 308.15 | 0.4432 | 1145.7 |
| 308.15 | 0.4957 | 1141.69 |
| 308.15 | 0.5486 | 1137.86 |
| 308.15 | 0.6486 | 1131.12 |
| 308.15 | 0.7501 | 1124.93 |
| 308.15 | 0.8489 | 1119.45 |
| 308.15 | 0.9400 | 1114.82 |
| 313.15 | 0.0465 | 1178.15 |
| 313.15 | 0.1495 | 1167.49 |
| 313.15 | 0.2501 | 1157.93 |
| 313.15 | 0.3505 | 1149.22 |
| 313.15 | 0.4432 | 1141.87 |
| 313.15 | 0.4957 | 1138.0 |
| 313.15 | 0.5486 | 1134.3 |
| 313.15 | 0.6486 | 1127.81 |
| 313.15 | 0.7501 | 1121.87 |
| 313.15 | 0.8489 | 1116.64 |
| 313.15 | 0.9400 | 1112.24 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0465 | 1470.0 |
| 298.15 | 0.1495 | 1486.0 |
| 298.15 | 0.2501 | 1502.0 |
| 298.15 | 0.3505 | 1518.0 |
| 298.15 | 0.4432 | 1532.0 |
| 298.15 | 0.4957 | 1541.0 |
| 298.15 | 0.5486 | 1550.0 |
| 298.15 | 0.6486 | 1565.0 |
| 298.15 | 0.7501 | 1581.0 |
| 298.15 | 0.8489 | 1594.0 |
| 298.15 | 0.9400 | 1604.0 |
| 308.15 | 0.0465 | 1432.0 |
| 308.15 | 0.1495 | 1450.0 |
| 308.15 | 0.2501 | 1468.0 |
| 308.15 | 0.3505 | 1485.0 |
| 308.15 | 0.4432 | 1502.0 |
| 308.15 | 0.4957 | 1510.0 |
| 308.15 | 0.5486 | 1521.0 |
| 308.15 | 0.6486 | 1535.0 |
| 308.15 | 0.7501 | 1550.0 |
| 308.15 | 0.8489 | 1567.0 |
| 308.15 | 0.9400 | 1576.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0465 | 1470.0 |
| 298.15 | 0.1495 | 1486.0 |
| 298.15 | 0.2501 | 1502.0 |
| 298.15 | 0.3505 | 1518.0 |
| 298.15 | 0.4432 | 1532.0 |
| 298.15 | 0.4957 | 1541.0 |
| 298.15 | 0.5486 | 1550.0 |
| 298.15 | 0.6486 | 1565.0 |
| 298.15 | 0.7501 | 1581.0 |
| 298.15 | 0.8489 | 1594.0 |
| 298.15 | 0.9400 | 1604.0 |
| 308.15 | 0.0465 | 1432.0 |
| 308.15 | 0.1495 | 1450.0 |
| 308.15 | 0.2501 | 1468.0 |
| 308.15 | 0.3505 | 1485.0 |
| 308.15 | 0.4432 | 1502.0 |
| 308.15 | 0.4957 | 1510.0 |
| 308.15 | 0.5486 | 1521.0 |
| 308.15 | 0.6486 | 1535.0 |
| 308.15 | 0.7501 | 1550.0 |
| 308.15 | 0.8489 | 1567.0 |
| 308.15 | 0.9400 | 1576.0 |