Mixture of Acetonitrile + Isopropyl acetate
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isopropyl acetate (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
333.15 |
0.0000 |
49.16 |
333.15 |
0.0468 |
49.99 |
333.15 |
0.1061 |
50.59 |
333.15 |
0.2038 |
51.28 |
333.15 |
0.3057 |
51.16 |
333.15 |
0.3193 |
51.37 |
333.15 |
0.3578 |
50.95 |
333.15 |
0.4002 |
50.86 |
333.15 |
0.5049 |
49.88 |
333.15 |
0.5870 |
48.89 |
333.15 |
0.7026 |
46.88 |
333.15 |
0.7928 |
45.10 |
333.15 |
0.8846 |
42.09 |
333.15 |
0.9407 |
40.12 |
333.15 |
1.0000 |
37.73 |
393.15 |
0.0000 |
297.37 |
393.15 |
0.0506 |
304.20 |
393.15 |
0.1035 |
308.68 |
393.15 |
0.1550 |
312.61 |
393.15 |
0.2566 |
315.43 |
393.15 |
0.2914 |
314.68 |
393.15 |
0.3623 |
315.09 |
393.15 |
0.3908 |
313.37 |
393.15 |
0.4912 |
310.40 |
393.15 |
0.5910 |
304.47 |
393.15 |
0.7015 |
294.82 |
393.15 |
0.7882 |
285.17 |
393.15 |
0.8944 |
270.07 |
393.15 |
0.9472 |
260.90 |
393.15 |
1.0000 |
249.59 |
453.15 |
0.0000 |
1096.90 |
453.15 |
0.0502 |
1117.30 |
453.15 |
0.1030 |
1133.10 |
453.15 |
0.1545 |
1142.70 |
453.15 |
0.2565 |
1152.50 |
453.15 |
0.2914 |
1153.00 |
453.15 |
0.3624 |
1151.20 |
453.15 |
0.3911 |
1147.20 |
453.15 |
0.4922 |
1136.20 |
453.15 |
0.5929 |
1114.70 |
453.15 |
0.7042 |
1082.10 |
453.15 |
0.7911 |
1049.70 |
453.15 |
0.8965 |
1001.10 |
453.15 |
0.9485 |
972.50 |
453.15 |
1.0000 |
939.90 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isopropyl acetate (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
333.15 |
0.0000 |
49.16 |
333.15 |
0.0468 |
49.99 |
333.15 |
0.1061 |
50.59 |
333.15 |
0.2038 |
51.28 |
333.15 |
0.3057 |
51.16 |
333.15 |
0.3193 |
51.37 |
333.15 |
0.3578 |
50.95 |
333.15 |
0.4002 |
50.86 |
333.15 |
0.5049 |
49.88 |
333.15 |
0.5870 |
48.89 |
333.15 |
0.7026 |
46.88 |
333.15 |
0.7928 |
45.10 |
333.15 |
0.8846 |
42.09 |
333.15 |
0.9407 |
40.12 |
333.15 |
1.0000 |
37.73 |
393.15 |
0.0000 |
297.37 |
393.15 |
0.0506 |
304.20 |
393.15 |
0.1035 |
308.68 |
393.15 |
0.1550 |
312.61 |
393.15 |
0.2566 |
315.43 |
393.15 |
0.2914 |
314.68 |
393.15 |
0.3623 |
315.09 |
393.15 |
0.3908 |
313.37 |
393.15 |
0.4912 |
310.40 |
393.15 |
0.5910 |
304.47 |
393.15 |
0.7015 |
294.82 |
393.15 |
0.7882 |
285.17 |
393.15 |
0.8944 |
270.07 |
393.15 |
0.9472 |
260.90 |
393.15 |
1.0000 |
249.59 |
453.15 |
0.0000 |
1096.90 |
453.15 |
0.0502 |
1117.30 |
453.15 |
0.1030 |
1133.10 |
453.15 |
0.1545 |
1142.70 |
453.15 |
0.2565 |
1152.50 |
453.15 |
0.2914 |
1153.00 |
453.15 |
0.3624 |
1151.20 |
453.15 |
0.3911 |
1147.20 |
453.15 |
0.4922 |
1136.20 |
453.15 |
0.5929 |
1114.70 |
453.15 |
0.7042 |
1082.10 |
453.15 |
0.7911 |
1049.70 |
453.15 |
0.8965 |
1001.10 |
453.15 |
0.9485 |
972.50 |
453.15 |
1.0000 |
939.90 |
Sources