Mixture of Hexane, tetradecafluoro- + Carbon dioxide

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. Vapor or sublimation pressure, kPa (2)
4. V_m - Molar volume, m3/mol (2)

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Carbon dioxide (2) - Gas
273.14	0.1597	0.9804
273.14	0.3195	0.9870
273.14	0.4702	0.9900
273.14	0.6096	0.9964
273.14	0.7598	0.9965
273.14	0.8901	0.9949
283.15	0.1532	0.9706
283.15	0.2680	0.9871
283.15	0.3911	0.9874
283.15	0.5243	0.9885
283.15	0.6200	0.9897
283.15	0.7257	0.9913
283.15	0.8464	0.9925
283.15	0.9494	0.9909
293.16	0.1221	0.9519
293.16	0.2307	0.9744
293.16	0.3410	0.9800
293.16	0.4509	0.9850
293.16	0.5415	0.9870
293.16	0.6505	0.9860
293.16	0.7214	0.9875
293.16	0.8014	0.9878
293.16	0.8703	0.9828
293.16	0.9368	0.9854
303.14	0.1100	0.9299
303.14	0.2104	0.9606
303.14	0.3074	0.9750
303.14	0.3937	0.9801
303.14	0.4735	0.9801
303.14	0.5475	0.9789
303.14	0.6168	0.9788
303.14	0.6828	0.9813
303.14	0.7477	0.9844
303.14	0.8086	0.9850
303.14	0.8678	0.9857
303.14	0.9065	0.9850
303.14	0.9575	0.9895
313.16	0.0962	0.8815
313.16	0.1885	0.9507
313.16	0.2740	0.9597
313.16	0.3518	0.9667
313.16	0.4248	0.9708
313.16	0.4925	0.9731
313.16	0.5550	0.9748
313.16	0.6158	0.9749
313.16	0.6721	0.9706
313.16	0.7253	0.9680
313.16	0.7744	0.9782
313.16	0.8220	0.9782
313.16	0.8670	0.9782
313.16	0.9290	0.9774
323.16	0.0907	0.8736
323.16	0.1684	0.9315
323.16	0.2484	0.9491
323.16	0.3200	0.9559
323.16	0.3867	0.9617
323.16	0.4491	0.9658
323.16	0.5073	0.9677
323.16	0.5624	0.9692
323.16	0.6138	0.9709
323.16	0.6631	0.9714
323.16	0.7091	0.9692
323.16	0.7523	0.9675
323.16	0.7945	0.9699
323.16	0.8332	0.9690
323.16	0.8738	0.9673
323.16	0.9032	0.9601
333.18	0.0791	0.7781
333.18	0.1498	0.8803
333.18	0.2228	0.9166
333.18	0.2899	0.9300
333.18	0.3536	0.9425
333.18	0.4181	0.9470
333.18	0.4735	0.9525
333.18	0.5253	0.9541
333.18	0.5744	0.9565
333.18	0.6208	0.9588
333.18	0.6655	0.9589
333.18	0.7031	0.9589
333.18	0.7537	0.9558
333.18	0.7942	0.9519
333.18	0.8195	0.9488
333.18	0.8602	0.9441
333.18	0.8976	0.9397

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Carbon dioxide (2) - Gas
273.14	0.1597	0.9804
273.14	0.3195	0.9870
273.14	0.4702	0.9900
273.14	0.6096	0.9964
273.14	0.7598	0.9965
273.14	0.8901	0.9949
283.15	0.1532	0.9706
283.15	0.2680	0.9871
283.15	0.3911	0.9874
283.15	0.5243	0.9885
283.15	0.6200	0.9897
283.15	0.7257	0.9913
283.15	0.8464	0.9925
283.15	0.9494	0.9909
293.16	0.1221	0.9519
293.16	0.2307	0.9744
293.16	0.3410	0.9800
293.16	0.4509	0.9850
293.16	0.5415	0.9870
293.16	0.6505	0.9860
293.16	0.7214	0.9875
293.16	0.8014	0.9878
293.16	0.8703	0.9828
293.16	0.9368	0.9854
303.14	0.1100	0.9299
303.14	0.2104	0.9606
303.14	0.3074	0.9750
303.14	0.3937	0.9801
303.14	0.4735	0.9801
303.14	0.5475	0.9789
303.14	0.6168	0.9788
303.14	0.6828	0.9813
303.14	0.7477	0.9844
303.14	0.8086	0.9850
303.14	0.8678	0.9857
303.14	0.9065	0.9850
303.14	0.9575	0.9895
313.16	0.0962	0.8815
313.16	0.1885	0.9507
313.16	0.2740	0.9597
313.16	0.3518	0.9667
313.16	0.4248	0.9708
313.16	0.4925	0.9731
313.16	0.5550	0.9748
313.16	0.6158	0.9749
313.16	0.6721	0.9706
313.16	0.7253	0.9680
313.16	0.7744	0.9782
313.16	0.8220	0.9782
313.16	0.8670	0.9782
313.16	0.9290	0.9774
323.16	0.0907	0.8736
323.16	0.1684	0.9315
323.16	0.2484	0.9491
323.16	0.3200	0.9559
323.16	0.3867	0.9617
323.16	0.4491	0.9658
323.16	0.5073	0.9677
323.16	0.5624	0.9692
323.16	0.6138	0.9709
323.16	0.6631	0.9714
323.16	0.7091	0.9692
323.16	0.7523	0.9675
323.16	0.7945	0.9699
323.16	0.8332	0.9690
323.16	0.8738	0.9673
323.16	0.9032	0.9601
333.18	0.0791	0.7781
333.18	0.1498	0.8803
333.18	0.2228	0.9166
333.18	0.2899	0.9300
333.18	0.3536	0.9425
333.18	0.4181	0.9470
333.18	0.4735	0.9525
333.18	0.5253	0.9541
333.18	0.5744	0.9565
333.18	0.6208	0.9588
333.18	0.6655	0.9589
333.18	0.7031	0.9589
333.18	0.7537	0.9558
333.18	0.7942	0.9519
333.18	0.8195	0.9488
333.18	0.8602	0.9441
333.18	0.8976	0.9397

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1460	690.00
0.1630	1210.00
0.2620	1720.00
0.2700	1450.00
0.3390	2250.00
0.4240	2770.00
0.4740	3280.00
0.5470	3790.00
0.6150	4320.00
0.6650	4860.00
0.7210	5330.00
0.7650	5590.00
0.7760	5860.00
0.8110	6200.00
0.8360	6420.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1460	690.00
0.1630	1210.00
0.2620	1720.00
0.2700	1450.00
0.3390	2250.00
0.4240	2770.00
0.4740	3280.00
0.5470	3790.00
0.6150	4320.00
0.6650	4860.00
0.7210	5330.00
0.7650	5590.00
0.7760	5860.00
0.8110	6200.00
0.8360	6420.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
273.14	0.1597	505.40
273.14	0.3195	1002.10
273.14	0.4702	1501.20
273.14	0.6096	2001.40
273.14	0.7598	2499.80
273.14	0.8901	2998.70
283.15	0.1532	501.30
283.15	0.2680	1000.80
283.15	0.3911	1501.40
283.15	0.5243	2001.60
283.15	0.6200	2498.10
283.15	0.7257	2999.20
283.15	0.8464	3500.30
283.15	0.9494	3999.50
293.16	0.1221	501.20
293.16	0.2307	999.50
293.16	0.3410	1499.40
293.16	0.4509	1999.30
293.16	0.5415	2499.90
293.16	0.6505	2999.60
293.16	0.7214	3503.20
293.16	0.8014	3998.70
293.16	0.8703	4500.50
293.16	0.9368	4998.70
303.14	0.1100	499.90
303.14	0.2104	997.40
303.14	0.3074	1508.00
303.14	0.3937	1998.80
303.14	0.4735	2498.70
303.14	0.5475	2997.50
303.14	0.6168	3500.70
303.14	0.6828	3995.10
303.14	0.7477	4499.80
303.14	0.8086	4998.60
303.14	0.8678	5498.90
303.14	0.9065	5998.90
303.14	0.9575	6509.50
313.16	0.0962	505.60
313.16	0.1885	1000.50
313.16	0.2740	1498.80
313.16	0.3518	1999.40
313.16	0.4248	2498.60
313.16	0.4925	2999.90
313.16	0.5550	3501.00
313.16	0.6158	4000.90
313.16	0.6721	4502.00
313.16	0.7253	5012.50
313.16	0.7744	5501.50
313.16	0.8220	5997.10
313.16	0.8670	6508.80
313.16	0.9290	7287.10
323.16	0.0907	502.80
323.16	0.1684	1001.50
323.16	0.2484	1498.80
323.16	0.3200	1998.40
323.16	0.3867	2499.10
323.16	0.4491	2999.50
323.16	0.5073	3498.90
323.16	0.5624	3996.90
323.16	0.6138	4498.60
323.16	0.6631	4999.20
323.16	0.7091	5498.80
323.16	0.7523	5997.10
323.16	0.7945	6500.20
323.16	0.8332	6999.30
323.16	0.8738	7501.30
323.16	0.9032	7917.90
333.18	0.0791	500.70
333.18	0.1498	1001.00
333.18	0.2228	1499.90
333.18	0.2899	1997.90
333.18	0.3536	2500.40
333.18	0.4181	2999.30
333.18	0.4735	3500.40
333.18	0.5253	3999.50
333.18	0.5744	4501.70
333.18	0.6208	5000.40
333.18	0.6655	5502.10
333.18	0.7031	6002.20
333.18	0.7537	6501.90
333.18	0.7942	7001.40
333.18	0.8195	7500.50
333.18	0.8602	7996.90
333.18	0.8976	8575.50

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
273.14	0.1597	505.40
273.14	0.3195	1002.10
273.14	0.4702	1501.20
273.14	0.6096	2001.40
273.14	0.7598	2499.80
273.14	0.8901	2998.70
283.15	0.1532	501.30
283.15	0.2680	1000.80
283.15	0.3911	1501.40
283.15	0.5243	2001.60
283.15	0.6200	2498.10
283.15	0.7257	2999.20
283.15	0.8464	3500.30
283.15	0.9494	3999.50
293.16	0.1221	501.20
293.16	0.2307	999.50
293.16	0.3410	1499.40
293.16	0.4509	1999.30
293.16	0.5415	2499.90
293.16	0.6505	2999.60
293.16	0.7214	3503.20
293.16	0.8014	3998.70
293.16	0.8703	4500.50
293.16	0.9368	4998.70
303.14	0.1100	499.90
303.14	0.2104	997.40
303.14	0.3074	1508.00
303.14	0.3937	1998.80
303.14	0.4735	2498.70
303.14	0.5475	2997.50
303.14	0.6168	3500.70
303.14	0.6828	3995.10
303.14	0.7477	4499.80
303.14	0.8086	4998.60
303.14	0.8678	5498.90
303.14	0.9065	5998.90
303.14	0.9575	6509.50
313.16	0.0962	505.60
313.16	0.1885	1000.50
313.16	0.2740	1498.80
313.16	0.3518	1999.40
313.16	0.4248	2498.60
313.16	0.4925	2999.90
313.16	0.5550	3501.00
313.16	0.6158	4000.90
313.16	0.6721	4502.00
313.16	0.7253	5012.50
313.16	0.7744	5501.50
313.16	0.8220	5997.10
313.16	0.8670	6508.80
313.16	0.9290	7287.10
323.16	0.0907	502.80
323.16	0.1684	1001.50
323.16	0.2484	1498.80
323.16	0.3200	1998.40
323.16	0.3867	2499.10
323.16	0.4491	2999.50
323.16	0.5073	3498.90
323.16	0.5624	3996.90
323.16	0.6138	4498.60
323.16	0.6631	4999.20
323.16	0.7091	5498.80
323.16	0.7523	5997.10
323.16	0.7945	6500.20
323.16	0.8332	6999.30
323.16	0.8738	7501.30
323.16	0.9032	7917.90
333.18	0.0791	500.70
333.18	0.1498	1001.00
333.18	0.2228	1499.90
333.18	0.2899	1997.90
333.18	0.3536	2500.40
333.18	0.4181	2999.30
333.18	0.4735	3500.40
333.18	0.5253	3999.50
333.18	0.5744	4501.70
333.18	0.6208	5000.40
333.18	0.6655	5502.10
333.18	0.7031	6002.20
333.18	0.7537	6501.90
333.18	0.7942	7001.40
333.18	0.8195	7500.50
333.18	0.8602	7996.90
333.18	0.8976	8575.50

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Molar volume, m3/mol - Liquid
0.1460	0.0002
0.1630	0.0002
0.2620	0.0002
0.2700	0.0002
0.3390	0.0002
0.4240	0.0002
0.4740	0.0001
0.5470	0.0001
0.6150	0.0001
0.6650	0.0001
0.7210	0.0001
0.7650	0.0001
0.7760	0.0001
0.8110	0.0001
0.8360	0.0001

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Molar volume, m3/mol - Liquid
0.1460	0.0002
0.1630	0.0002
0.2620	0.0002
0.2700	0.0002
0.3390	0.0002
0.4240	0.0002
0.4740	0.0001
0.5470	0.0001
0.6150	0.0001
0.6650	0.0001
0.7210	0.0001
0.7650	0.0001
0.7760	0.0001
0.8110	0.0001
0.8360	0.0001

Sources

• New experimental VLE data for the binary mixture of carbon dioxide + perfluorohexane (CO2 + C6F14) from 273 K to 333 K
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems