Datasets
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Mole fraction (12)
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 293.15 |
22.00 |
0.8195 |
| 303.15 |
35.00 |
0.8213 |
| 313.15 |
43.00 |
0.8225 |
| 323.15 |
61.00 |
0.8088 |
| 333.15 |
67.00 |
0.8163 |
| 343.15 |
96.00 |
0.7954 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 293.15 |
22.00 |
0.0305 |
| 303.15 |
35.00 |
0.0229 |
| 313.15 |
43.00 |
0.0195 |
| 323.15 |
61.00 |
0.0158 |
| 333.15 |
67.00 |
0.0147 |
| 343.15 |
96.00 |
0.0114 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 293.15 |
22.00 |
0.8478 |
| 303.15 |
35.00 |
0.8328 |
| 333.15 |
67.00 |
0.8205 |
| 363.15 |
194.00 |
0.8376 |
| 393.15 |
471.00 |
0.8029 |
| 423.15 |
965.00 |
0.7756 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 293.15 |
22.00 |
0.0249 |
| 303.15 |
35.00 |
0.0274 |
| 333.15 |
67.00 |
0.0118 |
| 363.15 |
194.00 |
0.0117 |
| 393.15 |
471.00 |
0.0095 |
| 423.15 |
965.00 |
0.0123 |
Mass fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 287.20 |
0.9657 |
| 288.50 |
0.9658 |
| 293.10 |
0.9655 |
| 293.60 |
0.9654 |
| 298.20 |
0.9651 |
| 298.70 |
0.9653 |
| 299.40 |
0.9627 |
| 302.60 |
0.9649 |
| 303.20 |
0.9650 |
| 307.60 |
0.9647 |
| 308.20 |
0.9643 |
| 312.50 |
0.9642 |
| 313.20 |
0.9642 |
| 317.60 |
0.9646 |
| 318.20 |
0.9644 |
| 322.10 |
0.9605 |
| 322.50 |
0.9633 |
| 323.20 |
0.9634 |
| 326.90 |
0.9633 |
| 328.20 |
0.9628 |
| 332.30 |
0.9621 |
| 333.20 |
0.9616 |
| 337.10 |
0.9605 |
| 338.20 |
0.9604 |
| 341.10 |
0.9619 |
| 342.30 |
0.9612 |
| 343.20 |
0.9606 |
Mass fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 287.20 |
0.1612 |
| 288.50 |
0.1598 |
| 293.10 |
0.1428 |
| 293.60 |
0.1455 |
| 298.20 |
0.1290 |
| 298.70 |
0.1286 |
| 299.40 |
0.1150 |
| 302.60 |
0.1162 |
| 303.20 |
0.1160 |
| 307.60 |
0.1043 |
| 308.20 |
0.1049 |
| 312.50 |
0.0966 |
| 313.20 |
0.0956 |
| 317.60 |
0.0869 |
| 318.20 |
0.0881 |
| 322.10 |
0.0701 |
| 322.50 |
0.0799 |
| 323.20 |
0.0794 |
| 326.90 |
0.0742 |
| 328.20 |
0.0741 |
| 332.30 |
0.0698 |
| 333.20 |
0.0693 |
| 337.10 |
0.0652 |
| 338.20 |
0.0651 |
| 341.10 |
0.0565 |
| 342.30 |
0.0619 |
| 343.20 |
0.0614 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 293.15 |
22.00 |
0.8195 |
| 303.15 |
35.00 |
0.8213 |
| 313.15 |
43.00 |
0.8225 |
| 323.15 |
61.00 |
0.8088 |
| 333.15 |
67.00 |
0.8163 |
| 343.15 |
96.00 |
0.7954 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 293.15 |
22.00 |
0.0305 |
| 303.15 |
35.00 |
0.0229 |
| 313.15 |
43.00 |
0.0195 |
| 323.15 |
61.00 |
0.0158 |
| 333.15 |
67.00 |
0.0147 |
| 343.15 |
96.00 |
0.0114 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 293.15 |
22.00 |
0.8478 |
| 303.15 |
35.00 |
0.8328 |
| 333.15 |
67.00 |
0.8205 |
| 363.15 |
194.00 |
0.8376 |
| 393.15 |
471.00 |
0.8029 |
| 423.15 |
965.00 |
0.7756 |
Mole fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 293.15 |
22.00 |
0.0249 |
| 303.15 |
35.00 |
0.0274 |
| 333.15 |
67.00 |
0.0118 |
| 363.15 |
194.00 |
0.0117 |
| 393.15 |
471.00 |
0.0095 |
| 423.15 |
965.00 |
0.0123 |
Mass fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 1 |
| 287.20 |
0.9657 |
| 288.50 |
0.9658 |
| 293.10 |
0.9655 |
| 293.60 |
0.9654 |
| 298.20 |
0.9651 |
| 298.70 |
0.9653 |
| 299.40 |
0.9627 |
| 302.60 |
0.9649 |
| 303.20 |
0.9650 |
| 307.60 |
0.9647 |
| 308.20 |
0.9643 |
| 312.50 |
0.9642 |
| 313.20 |
0.9642 |
| 317.60 |
0.9646 |
| 318.20 |
0.9644 |
| 322.10 |
0.9605 |
| 322.50 |
0.9633 |
| 323.20 |
0.9634 |
| 326.90 |
0.9633 |
| 328.20 |
0.9628 |
| 332.30 |
0.9621 |
| 333.20 |
0.9616 |
| 337.10 |
0.9605 |
| 338.20 |
0.9604 |
| 341.10 |
0.9619 |
| 342.30 |
0.9612 |
| 343.20 |
0.9606 |
Mass fraction of Furan, tetrahydro-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Furan, tetrahydro-2-methyl- (2) - Liquid mixture 2 |
| 287.20 |
0.1612 |
| 288.50 |
0.1598 |
| 293.10 |
0.1428 |
| 293.60 |
0.1455 |
| 298.20 |
0.1290 |
| 298.70 |
0.1286 |
| 299.40 |
0.1150 |
| 302.60 |
0.1162 |
| 303.20 |
0.1160 |
| 307.60 |
0.1043 |
| 308.20 |
0.1049 |
| 312.50 |
0.0966 |
| 313.20 |
0.0956 |
| 317.60 |
0.0869 |
| 318.20 |
0.0881 |
| 322.10 |
0.0701 |
| 322.50 |
0.0799 |
| 323.20 |
0.0794 |
| 326.90 |
0.0742 |
| 328.20 |
0.0741 |
| 332.30 |
0.0698 |
| 333.20 |
0.0693 |
| 337.10 |
0.0652 |
| 338.20 |
0.0651 |
| 341.10 |
0.0565 |
| 342.30 |
0.0619 |
| 343.20 |
0.0614 |
Sources
