Mixture of Carbon dioxide + Ethanol + Thiophene
Datasets
-
Mole fraction (4)
Mole fraction of Thiophene (3)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Thiophene (3) - Gas |
333.90 |
2527.00 |
0.9714 |
0.0232 |
333.90 |
3001.00 |
0.9748 |
0.0205 |
333.90 |
3899.00 |
0.9789 |
0.0173 |
333.90 |
5035.00 |
0.9802 |
0.0164 |
333.90 |
6048.00 |
0.9794 |
0.0173 |
333.90 |
7081.00 |
0.9776 |
0.0191 |
333.90 |
7744.00 |
0.9763 |
0.0211 |
333.90 |
8392.00 |
0.9733 |
0.0234 |
363.17 |
2450.00 |
0.8900 |
0.1043 |
363.17 |
3995.00 |
0.9290 |
0.0645 |
363.17 |
5455.00 |
0.9531 |
0.0397 |
363.17 |
7002.00 |
0.9571 |
0.0353 |
363.17 |
8105.00 |
0.9551 |
0.0365 |
363.17 |
9059.00 |
0.9531 |
0.0381 |
363.17 |
10038.00 |
0.9458 |
0.0439 |
363.17 |
11028.00 |
0.9370 |
0.0507 |
363.17 |
11385.00 |
0.9333 |
0.0536 |
363.29 |
2034.00 |
0.9328 |
0.0667 |
363.29 |
3548.00 |
0.9506 |
0.0473 |
363.29 |
5131.00 |
0.9590 |
0.0399 |
363.29 |
7039.00 |
0.9597 |
0.0372 |
363.29 |
8027.00 |
0.9575 |
0.0390 |
363.29 |
8854.00 |
0.9554 |
0.0408 |
363.29 |
9764.00 |
0.9515 |
0.0442 |
363.29 |
10792.00 |
0.9441 |
0.0508 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Thiophene (3) - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Thiophene (3) - Gas |
333.84 |
2009.00 |
0.7432 |
0.1329 |
0.9641 |
0.0307 |
333.84 |
3172.00 |
0.6709 |
0.2153 |
0.9712 |
0.0207 |
333.84 |
4834.00 |
0.5500 |
0.3465 |
0.9751 |
0.0175 |
333.84 |
6090.00 |
0.4486 |
0.4645 |
0.9750 |
0.0179 |
333.84 |
7125.00 |
0.3591 |
0.5710 |
0.9734 |
0.0194 |
333.84 |
8147.00 |
0.2689 |
0.6785 |
0.9712 |
0.0215 |
334.30 |
2056.00 |
0.7208 |
0.1392 |
0.9644 |
0.0249 |
334.30 |
3024.00 |
0.6523 |
0.2162 |
0.9718 |
0.0200 |
334.30 |
4037.00 |
0.5840 |
0.2967 |
0.9748 |
0.0181 |
334.30 |
5002.00 |
0.5084 |
0.3843 |
0.9756 |
0.0178 |
334.30 |
5639.00 |
0.4976 |
0.4382 |
0.9767 |
0.0182 |
334.30 |
6347.00 |
0.3861 |
0.5279 |
0.9758 |
0.0182 |
334.30 |
6801.00 |
0.3605 |
0.5734 |
0.9752 |
0.0191 |
334.30 |
7410.00 |
0.2941 |
0.6382 |
0.9639 |
0.0285 |
363.64 |
1852.00 |
0.8797 |
0.1092 |
0.9206 |
0.0754 |
363.64 |
4795.00 |
0.7363 |
0.2388 |
0.9528 |
0.0419 |
363.64 |
6238.00 |
0.6217 |
0.3458 |
0.9559 |
0.0383 |
363.64 |
7700.00 |
0.5090 |
0.4516 |
0.9545 |
0.0386 |
363.64 |
9003.00 |
0.3926 |
0.5530 |
0.9474 |
0.0424 |
Mole fraction of Thiophene (3)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Thiophene (3) - Gas |
333.90 |
2527.00 |
0.9714 |
0.0232 |
333.90 |
3001.00 |
0.9748 |
0.0205 |
333.90 |
3899.00 |
0.9789 |
0.0173 |
333.90 |
5035.00 |
0.9802 |
0.0164 |
333.90 |
6048.00 |
0.9794 |
0.0173 |
333.90 |
7081.00 |
0.9776 |
0.0191 |
333.90 |
7744.00 |
0.9763 |
0.0211 |
333.90 |
8392.00 |
0.9733 |
0.0234 |
363.17 |
2450.00 |
0.8900 |
0.1043 |
363.17 |
3995.00 |
0.9290 |
0.0645 |
363.17 |
5455.00 |
0.9531 |
0.0397 |
363.17 |
7002.00 |
0.9571 |
0.0353 |
363.17 |
8105.00 |
0.9551 |
0.0365 |
363.17 |
9059.00 |
0.9531 |
0.0381 |
363.17 |
10038.00 |
0.9458 |
0.0439 |
363.17 |
11028.00 |
0.9370 |
0.0507 |
363.17 |
11385.00 |
0.9333 |
0.0536 |
363.29 |
2034.00 |
0.9328 |
0.0667 |
363.29 |
3548.00 |
0.9506 |
0.0473 |
363.29 |
5131.00 |
0.9590 |
0.0399 |
363.29 |
7039.00 |
0.9597 |
0.0372 |
363.29 |
8027.00 |
0.9575 |
0.0390 |
363.29 |
8854.00 |
0.9554 |
0.0408 |
363.29 |
9764.00 |
0.9515 |
0.0442 |
363.29 |
10792.00 |
0.9441 |
0.0508 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Thiophene (3) - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Thiophene (3) - Gas |
333.84 |
2009.00 |
0.7432 |
0.1329 |
0.9641 |
0.0307 |
333.84 |
3172.00 |
0.6709 |
0.2153 |
0.9712 |
0.0207 |
333.84 |
4834.00 |
0.5500 |
0.3465 |
0.9751 |
0.0175 |
333.84 |
6090.00 |
0.4486 |
0.4645 |
0.9750 |
0.0179 |
333.84 |
7125.00 |
0.3591 |
0.5710 |
0.9734 |
0.0194 |
333.84 |
8147.00 |
0.2689 |
0.6785 |
0.9712 |
0.0215 |
334.30 |
2056.00 |
0.7208 |
0.1392 |
0.9644 |
0.0249 |
334.30 |
3024.00 |
0.6523 |
0.2162 |
0.9718 |
0.0200 |
334.30 |
4037.00 |
0.5840 |
0.2967 |
0.9748 |
0.0181 |
334.30 |
5002.00 |
0.5084 |
0.3843 |
0.9756 |
0.0178 |
334.30 |
5639.00 |
0.4976 |
0.4382 |
0.9767 |
0.0182 |
334.30 |
6347.00 |
0.3861 |
0.5279 |
0.9758 |
0.0182 |
334.30 |
6801.00 |
0.3605 |
0.5734 |
0.9752 |
0.0191 |
334.30 |
7410.00 |
0.2941 |
0.6382 |
0.9639 |
0.0285 |
363.64 |
1852.00 |
0.8797 |
0.1092 |
0.9206 |
0.0754 |
363.64 |
4795.00 |
0.7363 |
0.2388 |
0.9528 |
0.0419 |
363.64 |
6238.00 |
0.6217 |
0.3458 |
0.9559 |
0.0383 |
363.64 |
7700.00 |
0.5090 |
0.4516 |
0.9545 |
0.0386 |
363.64 |
9003.00 |
0.3926 |
0.5530 |
0.9474 |
0.0424 |
Sources