Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0473 | 0.0009 |
298.15 | 0.1490 | 0.0015 |
298.15 | 0.2493 | 0.0023 |
298.15 | 0.3495 | 0.0035 |
298.15 | 0.4390 | 0.0050 |
298.15 | 0.4734 | 0.0057 |
298.15 | 0.5509 | 0.0077 |
298.15 | 0.6512 | 0.0111 |
298.15 | 0.7493 | 0.0156 |
298.15 | 0.8483 | 0.0216 |
298.15 | 0.9428 | 0.0290 |
308.15 | 0.0473 | 0.0008 |
308.15 | 0.1490 | 0.0012 |
308.15 | 0.2493 | 0.0017 |
308.15 | 0.3495 | 0.0024 |
308.15 | 0.4390 | 0.0033 |
308.15 | 0.4734 | 0.0037 |
308.15 | 0.5509 | 0.0048 |
308.15 | 0.6512 | 0.0068 |
308.15 | 0.7493 | 0.0094 |
308.15 | 0.8483 | 0.0131 |
308.15 | 0.9428 | 0.0177 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Triethylene glycol (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0473 | 0.0009 |
298.15 | 0.1490 | 0.0015 |
298.15 | 0.2493 | 0.0023 |
298.15 | 0.3495 | 0.0035 |
298.15 | 0.4390 | 0.0050 |
298.15 | 0.4734 | 0.0057 |
298.15 | 0.5509 | 0.0077 |
298.15 | 0.6512 | 0.0111 |
298.15 | 0.7493 | 0.0156 |
298.15 | 0.8483 | 0.0216 |
298.15 | 0.9428 | 0.0290 |
308.15 | 0.0473 | 0.0008 |
308.15 | 0.1490 | 0.0012 |
308.15 | 0.2493 | 0.0017 |
308.15 | 0.3495 | 0.0024 |
308.15 | 0.4390 | 0.0033 |
308.15 | 0.4734 | 0.0037 |
308.15 | 0.5509 | 0.0048 |
308.15 | 0.6512 | 0.0068 |
308.15 | 0.7493 | 0.0094 |
308.15 | 0.8483 | 0.0131 |
308.15 | 0.9428 | 0.0177 |
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 | 0.0473 | 1102.31 |
298.15 | 0.1490 | 1105.2 |
298.15 | 0.2493 | 1107.74 |
298.15 | 0.3495 | 1110.02 |
298.15 | 0.4390 | 1111.86 |
298.15 | 0.4734 | 1112.52 |
298.15 | 0.5509 | 1113.91 |
298.15 | 0.6512 | 1115.53 |
298.15 | 0.7493 | 1116.92 |
298.15 | 0.8483 | 1118.13 |
298.15 | 0.9428 | 1119.1 |
303.15 | 0.0473 | 1097.01 |
303.15 | 0.1490 | 1100.08 |
303.15 | 0.2493 | 1102.8 |
303.15 | 0.3495 | 1105.25 |
303.15 | 0.4390 | 1107.24 |
303.15 | 0.4734 | 1107.96 |
303.15 | 0.5509 | 1109.48 |
303.15 | 0.6512 | 1111.26 |
303.15 | 0.7493 | 1112.81 |
303.15 | 0.8483 | 1114.18 |
303.15 | 0.9428 | 1115.3 |
308.15 | 0.0473 | 1091.35 |
308.15 | 0.1490 | 1094.63 |
308.15 | 0.2493 | 1097.55 |
308.15 | 0.3495 | 1100.19 |
308.15 | 0.4390 | 1102.35 |
308.15 | 0.4734 | 1103.13 |
308.15 | 0.5509 | 1104.79 |
308.15 | 0.6512 | 1106.75 |
308.15 | 0.7493 | 1108.47 |
308.15 | 0.8483 | 1110.01 |
308.15 | 0.9428 | 1111.28 |
313.15 | 0.0473 | 1086.48 |
313.15 | 0.1490 | 1090.07 |
313.15 | 0.2493 | 1093.28 |
313.15 | 0.3495 | 1096.19 |
313.15 | 0.4390 | 1098.58 |
313.15 | 0.4734 | 1099.44 |
313.15 | 0.5509 | 1101.3 |
313.15 | 0.6512 | 1103.51 |
313.15 | 0.7493 | 1105.47 |
313.15 | 0.8483 | 1107.24 |
313.15 | 0.9428 | 1108.73 |
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 | 0.0473 | 1102.31 |
298.15 | 0.1490 | 1105.2 |
298.15 | 0.2493 | 1107.74 |
298.15 | 0.3495 | 1110.02 |
298.15 | 0.4390 | 1111.86 |
298.15 | 0.4734 | 1112.52 |
298.15 | 0.5509 | 1113.91 |
298.15 | 0.6512 | 1115.53 |
298.15 | 0.7493 | 1116.92 |
298.15 | 0.8483 | 1118.13 |
298.15 | 0.9428 | 1119.1 |
303.15 | 0.0473 | 1097.01 |
303.15 | 0.1490 | 1100.08 |
303.15 | 0.2493 | 1102.8 |
303.15 | 0.3495 | 1105.25 |
303.15 | 0.4390 | 1107.24 |
303.15 | 0.4734 | 1107.96 |
303.15 | 0.5509 | 1109.48 |
303.15 | 0.6512 | 1111.26 |
303.15 | 0.7493 | 1112.81 |
303.15 | 0.8483 | 1114.18 |
303.15 | 0.9428 | 1115.3 |
308.15 | 0.0473 | 1091.35 |
308.15 | 0.1490 | 1094.63 |
308.15 | 0.2493 | 1097.55 |
308.15 | 0.3495 | 1100.19 |
308.15 | 0.4390 | 1102.35 |
308.15 | 0.4734 | 1103.13 |
308.15 | 0.5509 | 1104.79 |
308.15 | 0.6512 | 1106.75 |
308.15 | 0.7493 | 1108.47 |
308.15 | 0.8483 | 1110.01 |
308.15 | 0.9428 | 1111.28 |
313.15 | 0.0473 | 1086.48 |
313.15 | 0.1490 | 1090.07 |
313.15 | 0.2493 | 1093.28 |
313.15 | 0.3495 | 1096.19 |
313.15 | 0.4390 | 1098.58 |
313.15 | 0.4734 | 1099.44 |
313.15 | 0.5509 | 1101.3 |
313.15 | 0.6512 | 1103.51 |
313.15 | 0.7493 | 1105.47 |
313.15 | 0.8483 | 1107.24 |
313.15 | 0.9428 | 1108.73 |
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 | 0.0473 | 1278.0 |
298.15 | 0.1490 | 1305.0 |
298.15 | 0.2493 | 1336.0 |
298.15 | 0.3495 | 1366.0 |
298.15 | 0.4390 | 1395.0 |
298.15 | 0.4734 | 1407.0 |
298.15 | 0.5509 | 1435.0 |
298.15 | 0.6512 | 1473.0 |
298.15 | 0.7493 | 1513.0 |
298.15 | 0.8483 | 1553.0 |
298.15 | 0.9428 | 1591.0 |
308.15 | 0.0473 | 1239.0 |
308.15 | 0.1490 | 1272.0 |
308.15 | 0.2493 | 1305.0 |
308.15 | 0.3495 | 1338.0 |
308.15 | 0.4390 | 1369.0 |
308.15 | 0.4734 | 1381.0 |
308.15 | 0.5509 | 1410.0 |
308.15 | 0.6512 | 1451.0 |
308.15 | 0.7493 | 1489.0 |
308.15 | 0.8483 | 1530.0 |
308.15 | 0.9428 | 1566.0 |
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 | 0.0473 | 1278.0 |
298.15 | 0.1490 | 1305.0 |
298.15 | 0.2493 | 1336.0 |
298.15 | 0.3495 | 1366.0 |
298.15 | 0.4390 | 1395.0 |
298.15 | 0.4734 | 1407.0 |
298.15 | 0.5509 | 1435.0 |
298.15 | 0.6512 | 1473.0 |
298.15 | 0.7493 | 1513.0 |
298.15 | 0.8483 | 1553.0 |
298.15 | 0.9428 | 1591.0 |
308.15 | 0.0473 | 1239.0 |
308.15 | 0.1490 | 1272.0 |
308.15 | 0.2493 | 1305.0 |
308.15 | 0.3495 | 1338.0 |
308.15 | 0.4390 | 1369.0 |
308.15 | 0.4734 | 1381.0 |
308.15 | 0.5509 | 1410.0 |
308.15 | 0.6512 | 1451.0 |
308.15 | 0.7493 | 1489.0 |
308.15 | 0.8483 | 1530.0 |
308.15 | 0.9428 | 1566.0 |