Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid mixture 1 |
---|---|
307.85 | 0.9705 |
312.55 | 0.9673 |
318.85 | 0.9640 |
323.64 | 0.9577 |
329.33 | 0.9542 |
334.85 | 0.9447 |
342.50 | 0.9313 |
349.40 | 0.9134 |
355.55 | 0.8838 |
365.25 | 0.8677 |
374.55 | 0.8426 |
383.75 | 0.8040 |
391.65 | 0.7784 |
399.65 | 0.7595 |
408.45 | 0.7401 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid mixture 2 |
---|---|
307.85 | 0.0193 |
312.55 | 0.0220 |
318.85 | 0.0248 |
323.64 | 0.0263 |
329.33 | 0.0273 |
334.85 | 0.0289 |
342.50 | 0.0298 |
349.40 | 0.0311 |
355.55 | 0.0316 |
365.25 | 0.0382 |
374.55 | 0.0417 |
383.75 | 0.0413 |
391.65 | 0.0428 |
399.65 | 0.0470 |
408.45 | 0.0504 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid mixture 1 |
---|---|
307.85 | 0.9705 |
312.55 | 0.9673 |
318.85 | 0.9640 |
323.64 | 0.9577 |
329.33 | 0.9542 |
334.85 | 0.9447 |
342.50 | 0.9313 |
349.40 | 0.9134 |
355.55 | 0.8838 |
365.25 | 0.8677 |
374.55 | 0.8426 |
383.75 | 0.8040 |
391.65 | 0.7784 |
399.65 | 0.7595 |
408.45 | 0.7401 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid mixture 2 |
---|---|
307.85 | 0.0193 |
312.55 | 0.0220 |
318.85 | 0.0248 |
323.64 | 0.0263 |
329.33 | 0.0273 |
334.85 | 0.0289 |
342.50 | 0.0298 |
349.40 | 0.0311 |
355.55 | 0.0316 |
365.25 | 0.0382 |
374.55 | 0.0417 |
383.75 | 0.0413 |
391.65 | 0.0428 |
399.65 | 0.0470 |
408.45 | 0.0504 |