Mixture of Carbon dioxide + Nitric oxide

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Nitric oxide (2) [ref]

Fixed		Measured
Mole fraction of Nitric oxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Nitric oxide (2) - Gas
0.0000	273.02	0.0000
0.0318	273.02	0.1656
0.0790	273.02	0.2948
0.0284	273.02	0.1514
0.0626	273.02	0.2605
0.0925	273.02	0.3192
0.1300	273.02	0.3636
0.1750	273.02	0.3897
0.2120	273.02	0.3945
0.2630	273.02	0.3806
0.0000	252.98	0.0000
0.0292	252.98	0.2622
0.0758	252.98	0.4500
0.1117	252.98	0.5168
0.1441	252.98	0.5535
0.1781	252.98	0.5787
0.2229	252.98	0.5988
0.2666	252.98	0.6062
0.3230	252.98	0.6018
0.3800	252.98	0.5875
0.4194	252.98	0.5715
0.0000	232.93	0.0000
0.0157	232.93	0.2841
0.0580	232.93	0.5629
0.1042	232.93	0.6669
0.1487	232.93	0.7126
0.1953	232.93	0.7390
0.2446	232.93	0.7550
0.2960	232.93	0.7610
0.3479	232.93	0.7661
0.4090	232.93	0.7610
0.4730	232.93	0.7430

Mole fraction of Nitric oxide (2) [ref]

Fixed		Measured
Mole fraction of Nitric oxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Nitric oxide (2) - Gas
0.0000	273.02	0.0000
0.0318	273.02	0.1656
0.0790	273.02	0.2948
0.0284	273.02	0.1514
0.0626	273.02	0.2605
0.0925	273.02	0.3192
0.1300	273.02	0.3636
0.1750	273.02	0.3897
0.2120	273.02	0.3945
0.2630	273.02	0.3806
0.0000	252.98	0.0000
0.0292	252.98	0.2622
0.0758	252.98	0.4500
0.1117	252.98	0.5168
0.1441	252.98	0.5535
0.1781	252.98	0.5787
0.2229	252.98	0.5988
0.2666	252.98	0.6062
0.3230	252.98	0.6018
0.3800	252.98	0.5875
0.4194	252.98	0.5715
0.0000	232.93	0.0000
0.0157	232.93	0.2841
0.0580	232.93	0.5629
0.1042	232.93	0.6669
0.1487	232.93	0.7126
0.1953	232.93	0.7390
0.2446	232.93	0.7550
0.2960	232.93	0.7610
0.3479	232.93	0.7661
0.4090	232.93	0.7610
0.4730	232.93	0.7430

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Nitric oxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	273.02	3505.00
0.0318	273.02	4554.00
0.0790	273.02	6005.00
0.0284	273.02	4439.00
0.0626	273.02	5514.00
0.0925	273.02	6427.00
0.1300	273.02	7423.00
0.1750	273.02	8516.00
0.2120	273.02	9298.00
0.2630	273.02	10081.00
0.0000	252.98	1979.90
0.0292	252.98	2901.00
0.0758	252.98	4332.00
0.1117	252.98	5328.00
0.1441	252.98	6187.00
0.1781	252.98	7047.00
0.2229	252.98	8082.00
0.2666	252.98	9005.00
0.3230	252.98	10090.00
0.3800	252.98	10992.00
0.4194	252.98	11486.00
0.0000	232.93	1009.90
0.0157	232.93	1483.00
0.0580	232.93	2700.00
0.1042	232.93	3910.00
0.1487	232.93	4980.00
0.1953	232.93	5999.00
0.2446	232.93	7008.00
0.2960	232.93	8008.00
0.3479	232.93	9009.00
0.4090	232.93	10082.00
0.4730	232.93	11208.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Nitric oxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	273.02	3505.00
0.0318	273.02	4554.00
0.0790	273.02	6005.00
0.0284	273.02	4439.00
0.0626	273.02	5514.00
0.0925	273.02	6427.00
0.1300	273.02	7423.00
0.1750	273.02	8516.00
0.2120	273.02	9298.00
0.2630	273.02	10081.00
0.0000	252.98	1979.90
0.0292	252.98	2901.00
0.0758	252.98	4332.00
0.1117	252.98	5328.00
0.1441	252.98	6187.00
0.1781	252.98	7047.00
0.2229	252.98	8082.00
0.2666	252.98	9005.00
0.3230	252.98	10090.00
0.3800	252.98	10992.00
0.4194	252.98	11486.00
0.0000	232.93	1009.90
0.0157	232.93	1483.00
0.0580	232.93	2700.00
0.1042	232.93	3910.00
0.1487	232.93	4980.00
0.1953	232.93	5999.00
0.2446	232.93	7008.00
0.2960	232.93	8008.00
0.3479	232.93	9009.00
0.4090	232.93	10082.00
0.4730	232.93	11208.00

Sources

• Thermodynamic Study of binary an ternary systems containing CO2 + impurities in the context of CO2 transportation