Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (2) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Triethylene glycol (2) - Liquid mixture 2 |
298.20 | 0.4888 | 0.4249 | 0.0021 | 0.0067 |
298.20 | 0.2855 | 0.6994 | 0.0024 | 0.0021 |
298.20 | 0.1203 | 0.8782 | 0.0028 | 0.0005 |
298.20 | 0.0805 | 0.9189 | 0.0031 | 0.0002 |
323.20 | 0.4797 | 0.4205 | 0.0046 | 0.0116 |
323.20 | 0.2694 | 0.7127 | 0.0049 | 0.0040 |
323.20 | 0.1112 | 0.8869 | 0.0054 | 0.0011 |
323.20 | 0.0726 | 0.9266 | 0.0058 | 0.0006 |
Operational condition: Pressure, kPa = 85 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Triethylene glycol (2) - Gas | Mole fraction of Water (3) - Liquid | Mole fraction of Triethylene glycol (2) - Liquid |
400.85 | 0.9978 | 0.0022 | 0.3730 | 0.6270 |
394.95 | 0.8222 | 0.0015 | 0.3679 | 0.6197 |
390.45 | 0.6564 | 0.0011 | 0.3590 | 0.6046 |
385.55 | 0.5707 | 0.0008 | 0.3496 | 0.5889 |
383.05 | 0.5482 | 0.0007 | 0.3463 | 0.5834 |
380.05 | 0.5180 | 0.0006 | 0.3403 | 0.5733 |
377.15 | 0.4952 | 0.0005 | 0.3346 | 0.5634 |
373.45 | 0.4680 | 0.0004 | 0.3254 | 0.5479 |
370.85 | 0.4396 | 0.0003 | 0.3084 | 0.5193 |
368.85 | 0.4104 | 0.0002 | 0.2666 | 0.4490 |
368.75 | 0.4026 | 0.0002 | 0.2348 | 0.3954 |
412.55 | 0.9945 | 0.0055 | 0.2510 | 0.7490 |
393.05 | 0.4821 | 0.0014 | 0.2290 | 0.6810 |
381.15 | 0.4008 | 0.0008 | 0.2108 | 0.6308 |
373.25 | 0.3673 | 0.0005 | 0.1990 | 0.5510 |
371.55 | 0.3427 | 0.0004 | 0.1703 | 0.5095 |
371.25 | 0.3352 | 0.0003 | 0.1536 | 0.4595 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (2) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Triethylene glycol (2) - Liquid mixture 2 |
298.20 | 0.4888 | 0.4249 | 0.0021 | 0.0067 |
298.20 | 0.2855 | 0.6994 | 0.0024 | 0.0021 |
298.20 | 0.1203 | 0.8782 | 0.0028 | 0.0005 |
298.20 | 0.0805 | 0.9189 | 0.0031 | 0.0002 |
323.20 | 0.4797 | 0.4205 | 0.0046 | 0.0116 |
323.20 | 0.2694 | 0.7127 | 0.0049 | 0.0040 |
323.20 | 0.1112 | 0.8869 | 0.0054 | 0.0011 |
323.20 | 0.0726 | 0.9266 | 0.0058 | 0.0006 |
Operational condition: Pressure, kPa = 85 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Triethylene glycol (2) - Gas | Mole fraction of Water (3) - Liquid | Mole fraction of Triethylene glycol (2) - Liquid |
400.85 | 0.9978 | 0.0022 | 0.3730 | 0.6270 |
394.95 | 0.8222 | 0.0015 | 0.3679 | 0.6197 |
390.45 | 0.6564 | 0.0011 | 0.3590 | 0.6046 |
385.55 | 0.5707 | 0.0008 | 0.3496 | 0.5889 |
383.05 | 0.5482 | 0.0007 | 0.3463 | 0.5834 |
380.05 | 0.5180 | 0.0006 | 0.3403 | 0.5733 |
377.15 | 0.4952 | 0.0005 | 0.3346 | 0.5634 |
373.45 | 0.4680 | 0.0004 | 0.3254 | 0.5479 |
370.85 | 0.4396 | 0.0003 | 0.3084 | 0.5193 |
368.85 | 0.4104 | 0.0002 | 0.2666 | 0.4490 |
368.75 | 0.4026 | 0.0002 | 0.2348 | 0.3954 |
412.55 | 0.9945 | 0.0055 | 0.2510 | 0.7490 |
393.05 | 0.4821 | 0.0014 | 0.2290 | 0.6810 |
381.15 | 0.4008 | 0.0008 | 0.2108 | 0.6308 |
373.25 | 0.3673 | 0.0005 | 0.1990 | 0.5510 |
371.55 | 0.3427 | 0.0004 | 0.1703 | 0.5095 |
371.25 | 0.3352 | 0.0003 | 0.1536 | 0.4595 |