Propane + Thiophene, tetrahydro-

Datasets

Operational condition: Temperature, K = 293.97 (Liquid)

Mole fraction of Propane (1) - Liquid	Mole fraction of Propane (1) - Gas
0.0104	0.9188
0.0231	0.9610
0.0339	0.9726
0.0913	0.9887
0.1266	0.9914
0.1782	0.9935
0.2264	0.9946
0.2760	0.9953
0.3278	0.9958
0.3799	0.9962
0.4324	0.9965
0.4849	0.9968
0.4879	0.9968
0.5365	0.9970
0.5852	0.9972
0.6348	0.9974
0.6847	0.9976
0.7346	0.9978
0.7828	0.9980
0.8387	0.9982
0.8911	0.9986
0.9441	0.9991
0.9864	0.9997

Operational condition: Temperature, K = 312.87 (Liquid)

Mole fraction of Propane (1) - Liquid	Mole fraction of Propane (1) - Gas
0.0058	0.7625
0.0243	0.9287
0.0369	0.9509
0.0763	0.9741
0.1180	0.9820
0.1621	0.9860
0.2119	0.9885
0.2621	0.9902
0.3125	0.9913
0.3649	0.9921
0.4190	0.9928
0.4768	0.9934
0.4785	0.9934
0.5251	0.9938
0.5722	0.9942
0.6205	0.9945
0.6697	0.9949
0.7228	0.9953
0.7747	0.9957
0.8268	0.9962
0.8824	0.9970
0.9405	0.9982
0.9629	0.9988
0.9827	0.9994

Operational condition: Temperature, K = 293.97 (Liquid)

Mole fraction of Propane (1) - Liquid	Mole fraction of Propane (1) - Gas
0.0104	0.9188
0.0231	0.9610
0.0339	0.9726
0.0913	0.9887
0.1266	0.9914
0.1782	0.9935
0.2264	0.9946
0.2760	0.9953
0.3278	0.9958
0.3799	0.9962
0.4324	0.9965
0.4849	0.9968
0.4879	0.9968
0.5365	0.9970
0.5852	0.9972
0.6348	0.9974
0.6847	0.9976
0.7346	0.9978
0.7828	0.9980
0.8387	0.9982
0.8911	0.9986
0.9441	0.9991
0.9864	0.9997

Operational condition: Temperature, K = 312.87 (Liquid)

Mole fraction of Propane (1) - Liquid	Mole fraction of Propane (1) - Gas
0.0058	0.7625
0.0243	0.9287
0.0369	0.9509
0.0763	0.9741
0.1180	0.9820
0.1621	0.9860
0.2119	0.9885
0.2621	0.9902
0.3125	0.9913
0.3649	0.9921
0.4190	0.9928
0.4768	0.9934
0.4785	0.9934
0.5251	0.9938
0.5722	0.9942
0.6205	0.9945
0.6697	0.9949
0.7228	0.9953
0.7747	0.9957
0.8268	0.9962
0.8824	0.9970
0.9405	0.9982
0.9629	0.9988
0.9827	0.9994

Operational condition: Temperature, K = 293.97 (Liquid)

Mole fraction of Propane (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	2.10
0.0104	53.80
0.0231	76.20
0.0339	185.00
0.0913	243.00
0.1266	317.40
0.1782	377.30
0.2264	429.80
0.2760	476.70
0.3278	516.80
0.3799	551.50
0.4324	581.20
0.4849	590.00
0.4879	613.90
0.5365	635.60
0.5852	656.30
0.6348	676.50
0.6847	697.00
0.7346	717.70
0.7828	744.60
0.8387	774.60
0.8911	812.00
0.9441	830.70
0.9864	848.30
1.0000	853.10

Operational condition: Temperature, K = 312.87 (Liquid)

Mole fraction of Propane (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	5.90
0.0058	25.20
0.0243	83.30
0.0369	120.70
0.0763	232.20
0.1180	337.50
0.1621	437.30
0.2119	535.70
0.2621	621.70
0.3125	697.00
0.3649	764.60
0.4190	825.20
0.4768	881.20
0.4785	884.60
0.5251	924.90
0.5722	962.10
0.6205	997.80
0.6697	1032.80
0.7228	1070.30
0.7747	1108.60
0.8268	1150.90
0.8824	1202.60
0.9405	1269.60
0.9629	1301.00
0.9827	1331.70
1.0000	1361.30

Operational condition: Temperature, K = 293.97 (Liquid)

Mole fraction of Propane (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	2.10
0.0104	53.80
0.0231	76.20
0.0339	185.00
0.0913	243.00
0.1266	317.40
0.1782	377.30
0.2264	429.80
0.2760	476.70
0.3278	516.80
0.3799	551.50
0.4324	581.20
0.4849	590.00
0.4879	613.90
0.5365	635.60
0.5852	656.30
0.6348	676.50
0.6847	697.00
0.7346	717.70
0.7828	744.60
0.8387	774.60
0.8911	812.00
0.9441	830.70
0.9864	848.30
1.0000	853.10

Operational condition: Temperature, K = 312.87 (Liquid)

Mole fraction of Propane (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	5.90
0.0058	25.20
0.0243	83.30
0.0369	120.70
0.0763	232.20
0.1180	337.50
0.1621	437.30
0.2119	535.70
0.2621	621.70
0.3125	697.00
0.3649	764.60
0.4190	825.20
0.4768	881.20
0.4785	884.60
0.5251	924.90
0.5722	962.10
0.6205	997.80
0.6697	1032.80
0.7228	1070.30
0.7747	1108.60
0.8268	1150.90
0.8824	1202.60
0.9405	1269.60
0.9629	1301.00
0.9827	1331.70
1.0000	1361.30