Mixture of Toluene + Carbon dioxide + Naphthalene
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Naphthalene (3)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Naphthalene (3) - Liquid |
298.15 |
960.00 |
0.1846 |
0.2564 |
298.15 |
1500.00 |
0.2065 |
0.2542 |
298.15 |
2000.00 |
0.2396 |
0.2496 |
298.15 |
2510.00 |
0.2824 |
0.2449 |
298.15 |
2950.00 |
0.3232 |
0.2353 |
298.15 |
3280.00 |
0.3576 |
0.2270 |
298.15 |
3520.00 |
0.3799 |
0.2224 |
298.15 |
3900.00 |
0.4153 |
0.2129 |
298.15 |
4420.00 |
0.4858 |
0.1836 |
298.15 |
4990.00 |
0.5949 |
0.1283 |
298.15 |
5370.00 |
0.6987 |
0.0932 |
298.15 |
5840.00 |
0.9198 |
0.0211 |
298.15 |
6120.00 |
0.9712 |
0.0096 |
308.15 |
1140.00 |
0.0908 |
0.3381 |
308.15 |
1860.00 |
0.1338 |
0.3312 |
308.15 |
2340.00 |
0.1823 |
0.3163 |
308.15 |
2810.00 |
0.2108 |
0.3043 |
308.15 |
3450.00 |
0.2723 |
0.2886 |
308.15 |
4170.00 |
0.3496 |
0.2661 |
308.15 |
4650.00 |
0.4154 |
0.2450 |
308.15 |
5310.00 |
0.4911 |
0.2262 |
308.15 |
5980.00 |
0.5669 |
0.1878 |
308.15 |
6570.00 |
0.6802 |
0.1261 |
308.15 |
6810.00 |
0.8592 |
0.0342 |
308.15 |
7180.00 |
0.9214 |
0.0198 |
308.15 |
7560.00 |
0.9884 |
0.0085 |
Mole fraction of Naphthalene (3)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Naphthalene (3) - Liquid |
298.15 |
960.00 |
0.1846 |
0.2564 |
298.15 |
1500.00 |
0.2065 |
0.2542 |
298.15 |
2000.00 |
0.2396 |
0.2496 |
298.15 |
2510.00 |
0.2824 |
0.2449 |
298.15 |
2950.00 |
0.3232 |
0.2353 |
298.15 |
3280.00 |
0.3576 |
0.2270 |
298.15 |
3520.00 |
0.3799 |
0.2224 |
298.15 |
3900.00 |
0.4153 |
0.2129 |
298.15 |
4420.00 |
0.4858 |
0.1836 |
298.15 |
4990.00 |
0.5949 |
0.1283 |
298.15 |
5370.00 |
0.6987 |
0.0932 |
298.15 |
5840.00 |
0.9198 |
0.0211 |
298.15 |
6120.00 |
0.9712 |
0.0096 |
308.15 |
1140.00 |
0.0908 |
0.3381 |
308.15 |
1860.00 |
0.1338 |
0.3312 |
308.15 |
2340.00 |
0.1823 |
0.3163 |
308.15 |
2810.00 |
0.2108 |
0.3043 |
308.15 |
3450.00 |
0.2723 |
0.2886 |
308.15 |
4170.00 |
0.3496 |
0.2661 |
308.15 |
4650.00 |
0.4154 |
0.2450 |
308.15 |
5310.00 |
0.4911 |
0.2262 |
308.15 |
5980.00 |
0.5669 |
0.1878 |
308.15 |
6570.00 |
0.6802 |
0.1261 |
308.15 |
6810.00 |
0.8592 |
0.0342 |
308.15 |
7180.00 |
0.9214 |
0.0198 |
308.15 |
7560.00 |
0.9884 |
0.0085 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Naphthalene (3) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
298.15 |
0.1846 |
0.2564 |
960.00 |
298.15 |
0.2065 |
0.2542 |
1500.00 |
298.15 |
0.2396 |
0.2496 |
2000.00 |
298.15 |
0.2824 |
0.2449 |
2510.00 |
298.15 |
0.3232 |
0.2353 |
2950.00 |
298.15 |
0.3576 |
0.2270 |
3280.00 |
298.15 |
0.3799 |
0.2224 |
3520.00 |
298.15 |
0.4153 |
0.2129 |
3900.00 |
298.15 |
0.4858 |
0.1836 |
4420.00 |
298.15 |
0.5949 |
0.1283 |
4990.00 |
298.15 |
0.6987 |
0.0932 |
5370.00 |
298.15 |
0.9198 |
0.0211 |
5840.00 |
298.15 |
0.9712 |
0.0096 |
6120.00 |
308.15 |
0.0908 |
0.3381 |
1140.00 |
308.15 |
0.1338 |
0.3312 |
1860.00 |
308.15 |
0.1823 |
0.3163 |
2340.00 |
308.15 |
0.2108 |
0.3043 |
2810.00 |
308.15 |
0.2723 |
0.2886 |
3450.00 |
308.15 |
0.3496 |
0.2661 |
4170.00 |
308.15 |
0.4154 |
0.2450 |
4650.00 |
308.15 |
0.4911 |
0.2262 |
5310.00 |
308.15 |
0.5669 |
0.1878 |
5980.00 |
308.15 |
0.6802 |
0.1261 |
6570.00 |
308.15 |
0.8592 |
0.0342 |
6810.00 |
308.15 |
0.9214 |
0.0198 |
7180.00 |
308.15 |
0.9884 |
0.0085 |
7560.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Naphthalene (3) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
298.15 |
0.1846 |
0.2564 |
960.00 |
298.15 |
0.2065 |
0.2542 |
1500.00 |
298.15 |
0.2396 |
0.2496 |
2000.00 |
298.15 |
0.2824 |
0.2449 |
2510.00 |
298.15 |
0.3232 |
0.2353 |
2950.00 |
298.15 |
0.3576 |
0.2270 |
3280.00 |
298.15 |
0.3799 |
0.2224 |
3520.00 |
298.15 |
0.4153 |
0.2129 |
3900.00 |
298.15 |
0.4858 |
0.1836 |
4420.00 |
298.15 |
0.5949 |
0.1283 |
4990.00 |
298.15 |
0.6987 |
0.0932 |
5370.00 |
298.15 |
0.9198 |
0.0211 |
5840.00 |
298.15 |
0.9712 |
0.0096 |
6120.00 |
308.15 |
0.0908 |
0.3381 |
1140.00 |
308.15 |
0.1338 |
0.3312 |
1860.00 |
308.15 |
0.1823 |
0.3163 |
2340.00 |
308.15 |
0.2108 |
0.3043 |
2810.00 |
308.15 |
0.2723 |
0.2886 |
3450.00 |
308.15 |
0.3496 |
0.2661 |
4170.00 |
308.15 |
0.4154 |
0.2450 |
4650.00 |
308.15 |
0.4911 |
0.2262 |
5310.00 |
308.15 |
0.5669 |
0.1878 |
5980.00 |
308.15 |
0.6802 |
0.1261 |
6570.00 |
308.15 |
0.8592 |
0.0342 |
6810.00 |
308.15 |
0.9214 |
0.0198 |
7180.00 |
308.15 |
0.9884 |
0.0085 |
7560.00 |
Sources