Datasets
-
Mole fraction (4)
-
Eutectic temperature, K (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Tfus - Solid-liquid equilibrium temperature, K (4)
Mole fraction of Propanoic acid (2)
[ref]
Fixed |
Measured |
Mole fraction of Propanoic acid (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Propanoic acid (2) - Gas |
0.0050 |
403.15 |
0.0330 |
0.0070 |
413.15 |
0.0290 |
0.0250 |
393.15 |
0.1110 |
0.0250 |
413.15 |
0.0930 |
0.0290 |
403.15 |
0.1520 |
0.0350 |
408.19 |
0.1330 |
0.0600 |
393.15 |
0.2350 |
0.0840 |
403.15 |
0.3340 |
0.0860 |
413.15 |
0.2550 |
0.1210 |
402.30 |
0.3510 |
0.1470 |
413.15 |
0.3820 |
0.1510 |
393.15 |
0.4570 |
0.1530 |
403.15 |
0.4720 |
0.2010 |
397.85 |
0.4980 |
0.2580 |
403.15 |
0.6130 |
0.2610 |
413.15 |
0.5680 |
0.2640 |
393.15 |
0.6150 |
0.2870 |
393.63 |
0.6280 |
0.3800 |
390.14 |
0.7180 |
0.4030 |
413.15 |
0.7140 |
0.4170 |
403.15 |
0.7560 |
0.4180 |
393.15 |
0.7610 |
0.4830 |
413.15 |
0.7690 |
0.5160 |
385.79 |
0.8210 |
0.5880 |
393.15 |
0.8590 |
0.5980 |
403.15 |
0.8540 |
0.6340 |
413.15 |
0.8610 |
0.6730 |
380.23 |
0.9040 |
0.7260 |
393.15 |
0.9160 |
0.7280 |
403.15 |
0.9110 |
0.7870 |
376.69 |
0.9410 |
0.7940 |
413.15 |
0.9300 |
0.8470 |
403.15 |
0.9530 |
0.8490 |
393.15 |
0.9560 |
0.8800 |
373.45 |
0.9670 |
0.8970 |
413.15 |
0.9670 |
0.9220 |
371.90 |
0.9790 |
0.9260 |
393.15 |
0.9780 |
0.9280 |
403.15 |
0.9750 |
0.9550 |
370.82 |
0.9870 |
0.9650 |
393.15 |
0.9900 |
0.9730 |
370.01 |
0.9920 |
0.9800 |
393.15 |
0.9940 |
0.9850 |
403.15 |
0.9940 |
0.9860 |
413.15 |
0.9950 |
0.9900 |
393.15 |
0.9970 |
0.9930 |
413.15 |
0.9980 |
0.9940 |
403.15 |
0.9980 |
Eutectic composition: mole fraction of Propanoic acid (2)
[ref]
Pressure, kPa - Liquid |
Eutectic composition: mole fraction of Propanoic acid (2) - Liquid |
84.50 |
0.5720 |
Mole fraction of Propanoic acid (2)
[ref]
Fixed |
Measured |
Mole fraction of Propanoic acid (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Propanoic acid (2) - Gas |
0.0050 |
403.15 |
0.0330 |
0.0070 |
413.15 |
0.0290 |
0.0250 |
393.15 |
0.1110 |
0.0250 |
413.15 |
0.0930 |
0.0290 |
403.15 |
0.1520 |
0.0350 |
408.19 |
0.1330 |
0.0600 |
393.15 |
0.2350 |
0.0840 |
403.15 |
0.3340 |
0.0860 |
413.15 |
0.2550 |
0.1210 |
402.30 |
0.3510 |
0.1470 |
413.15 |
0.3820 |
0.1510 |
393.15 |
0.4570 |
0.1530 |
403.15 |
0.4720 |
0.2010 |
397.85 |
0.4980 |
0.2580 |
403.15 |
0.6130 |
0.2610 |
413.15 |
0.5680 |
0.2640 |
393.15 |
0.6150 |
0.2870 |
393.63 |
0.6280 |
0.3800 |
390.14 |
0.7180 |
0.4030 |
413.15 |
0.7140 |
0.4170 |
403.15 |
0.7560 |
0.4180 |
393.15 |
0.7610 |
0.4830 |
413.15 |
0.7690 |
0.5160 |
385.79 |
0.8210 |
0.5880 |
393.15 |
0.8590 |
0.5980 |
403.15 |
0.8540 |
0.6340 |
413.15 |
0.8610 |
0.6730 |
380.23 |
0.9040 |
0.7260 |
393.15 |
0.9160 |
0.7280 |
403.15 |
0.9110 |
0.7870 |
376.69 |
0.9410 |
0.7940 |
413.15 |
0.9300 |
0.8470 |
403.15 |
0.9530 |
0.8490 |
393.15 |
0.9560 |
0.8800 |
373.45 |
0.9670 |
0.8970 |
413.15 |
0.9670 |
0.9220 |
371.90 |
0.9790 |
0.9260 |
393.15 |
0.9780 |
0.9280 |
403.15 |
0.9750 |
0.9550 |
370.82 |
0.9870 |
0.9650 |
393.15 |
0.9900 |
0.9730 |
370.01 |
0.9920 |
0.9800 |
393.15 |
0.9940 |
0.9850 |
403.15 |
0.9940 |
0.9860 |
413.15 |
0.9950 |
0.9900 |
393.15 |
0.9970 |
0.9930 |
413.15 |
0.9980 |
0.9940 |
403.15 |
0.9980 |
Eutectic composition: mole fraction of Propanoic acid (2)
[ref]
Pressure, kPa - Liquid |
Eutectic composition: mole fraction of Propanoic acid (2) - Liquid |
84.50 |
0.5720 |
Eutectic temperature, K
[ref]
Pressure, kPa - Liquid |
Eutectic temperature, K - Liquid |
84.50 |
215.00 |
Eutectic temperature, K
[ref]
Pressure, kPa - Liquid |
Eutectic temperature, K - Liquid |
84.50 |
215.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Propanoic acid (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0050 |
403.15 |
15.23 |
0.0070 |
413.15 |
22.24 |
0.0250 |
393.15 |
10.78 |
0.0250 |
413.15 |
23.35 |
0.0290 |
403.15 |
16.51 |
0.0600 |
393.15 |
12.05 |
0.0840 |
403.15 |
18.78 |
0.0860 |
413.15 |
27.33 |
0.1470 |
413.15 |
30.85 |
0.1510 |
393.15 |
15.21 |
0.1530 |
403.15 |
21.31 |
0.2580 |
403.15 |
26.20 |
0.2610 |
413.15 |
38.41 |
0.2640 |
393.15 |
18.73 |
0.4030 |
413.15 |
48.71 |
0.4170 |
403.15 |
34.64 |
0.4180 |
393.15 |
24.49 |
0.4830 |
413.15 |
54.24 |
0.5880 |
393.15 |
31.56 |
0.5980 |
403.15 |
44.90 |
0.6340 |
413.15 |
65.90 |
0.7260 |
393.15 |
37.51 |
0.7280 |
403.15 |
52.25 |
0.7940 |
413.15 |
78.93 |
0.8470 |
403.15 |
60.04 |
0.8490 |
393.15 |
43.13 |
0.8970 |
413.15 |
88.90 |
0.9260 |
393.15 |
46.92 |
0.9280 |
403.15 |
65.80 |
0.9650 |
393.15 |
48.16 |
0.9800 |
393.15 |
48.76 |
0.9850 |
403.15 |
68.85 |
0.9860 |
413.15 |
96.10 |
0.9900 |
393.15 |
49.48 |
0.9930 |
413.15 |
97.72 |
0.9940 |
403.15 |
69.87 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Propanoic acid (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0050 |
403.15 |
15.23 |
0.0070 |
413.15 |
22.24 |
0.0250 |
393.15 |
10.78 |
0.0250 |
413.15 |
23.35 |
0.0290 |
403.15 |
16.51 |
0.0600 |
393.15 |
12.05 |
0.0840 |
403.15 |
18.78 |
0.0860 |
413.15 |
27.33 |
0.1470 |
413.15 |
30.85 |
0.1510 |
393.15 |
15.21 |
0.1530 |
403.15 |
21.31 |
0.2580 |
403.15 |
26.20 |
0.2610 |
413.15 |
38.41 |
0.2640 |
393.15 |
18.73 |
0.4030 |
413.15 |
48.71 |
0.4170 |
403.15 |
34.64 |
0.4180 |
393.15 |
24.49 |
0.4830 |
413.15 |
54.24 |
0.5880 |
393.15 |
31.56 |
0.5980 |
403.15 |
44.90 |
0.6340 |
413.15 |
65.90 |
0.7260 |
393.15 |
37.51 |
0.7280 |
403.15 |
52.25 |
0.7940 |
413.15 |
78.93 |
0.8470 |
403.15 |
60.04 |
0.8490 |
393.15 |
43.13 |
0.8970 |
413.15 |
88.90 |
0.9260 |
393.15 |
46.92 |
0.9280 |
403.15 |
65.80 |
0.9650 |
393.15 |
48.16 |
0.9800 |
393.15 |
48.76 |
0.9850 |
403.15 |
68.85 |
0.9860 |
413.15 |
96.10 |
0.9900 |
393.15 |
49.48 |
0.9930 |
413.15 |
97.72 |
0.9940 |
403.15 |
69.87 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
20 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0350 |
408.19 |
0.1210 |
402.30 |
0.2010 |
397.85 |
0.2870 |
393.63 |
0.3800 |
390.14 |
0.5160 |
385.79 |
0.6730 |
380.23 |
0.7870 |
376.69 |
0.8800 |
373.45 |
0.9220 |
371.90 |
0.9550 |
370.82 |
0.9730 |
370.01 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
20 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0350 |
408.19 |
0.1210 |
402.30 |
0.2010 |
397.85 |
0.2870 |
393.63 |
0.3800 |
390.14 |
0.5160 |
385.79 |
0.6730 |
380.23 |
0.7870 |
376.69 |
0.8800 |
373.45 |
0.9220 |
371.90 |
0.9550 |
370.82 |
0.9730 |
370.01 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
239.00 |
0.0960 |
234.00 |
0.0960 |
234.00 |
0.1580 |
231.00 |
0.1580 |
231.00 |
0.2180 |
228.00 |
0.2180 |
228.00 |
0.2740 |
225.00 |
0.2740 |
226.00 |
0.3370 |
223.00 |
0.4260 |
219.00 |
0.5260 |
215.00 |
0.5260 |
215.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.5650 |
219.00 |
0.6210 |
223.00 |
0.6780 |
227.00 |
0.7280 |
232.00 |
0.8000 |
238.00 |
0.8670 |
240.00 |
0.9260 |
246.00 |
0.9950 |
252.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
239.00 |
0.0960 |
234.00 |
0.0960 |
234.00 |
0.1580 |
231.00 |
0.1580 |
231.00 |
0.2180 |
228.00 |
0.2180 |
228.00 |
0.2740 |
225.00 |
0.2740 |
226.00 |
0.3370 |
223.00 |
0.4260 |
219.00 |
0.5260 |
215.00 |
0.5260 |
215.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Mole fraction of Propanoic acid (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.5650 |
219.00 |
0.6210 |
223.00 |
0.6780 |
227.00 |
0.7280 |
232.00 |
0.8000 |
238.00 |
0.8670 |
240.00 |
0.9260 |
246.00 |
0.9950 |
252.00 |
Sources