Mixture of Nitric oxide + Butane, decafluoro-

Datasets

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

Mole fraction of Nitric oxide (1) [ref]

Fixed		Measured
Mole fraction of Nitric oxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Nitric oxide (1) - Gas
0.0730	292.97	0.8230
0.0940	292.97	0.8490
0.1300	292.97	0.8790
0.1530	292.97	0.8880
0.2040	292.97	0.9050
0.2780	292.97	0.9100
0.3520	292.97	0.9080
0.4010	292.97	0.9000
0.4450	292.97	0.8940
0.4950	292.97	0.8880
0.5720	292.97	0.8740
0.6750	292.97	0.8320
0.7300	292.97	0.7870
0.0330	312.93	0.5240
0.0780	312.93	0.7220
0.1260	312.93	0.7930
0.1750	312.93	0.8110
0.2290	312.93	0.8350
0.3080	312.93	0.8450
0.3600	312.93	0.8450
0.4200	312.93	0.8410
0.5070	312.93	0.8250
0.6360	312.93	0.7960
0.0440	332.97	0.4470
0.0800	332.97	0.5750
0.1250	332.97	0.6520
0.1630	332.97	0.6980
0.2020	332.97	0.7190
0.2440	332.97	0.7360
0.3060	332.97	0.7450
0.3760	332.97	0.7360
0.4350	332.97	0.7210
0.4950	332.97	0.7050

Mole fraction of Nitric oxide (1) [ref]

Fixed		Measured
Mole fraction of Nitric oxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Nitric oxide (1) - Gas
0.0730	292.97	0.8230
0.0940	292.97	0.8490
0.1300	292.97	0.8790
0.1530	292.97	0.8880
0.2040	292.97	0.9050
0.2780	292.97	0.9100
0.3520	292.97	0.9080
0.4010	292.97	0.9000
0.4450	292.97	0.8940
0.4950	292.97	0.8880
0.5720	292.97	0.8740
0.6750	292.97	0.8320
0.7300	292.97	0.7870
0.0330	312.93	0.5240
0.0780	312.93	0.7220
0.1260	312.93	0.7930
0.1750	312.93	0.8110
0.2290	312.93	0.8350
0.3080	312.93	0.8450
0.3600	312.93	0.8450
0.4200	312.93	0.8410
0.5070	312.93	0.8250
0.6360	312.93	0.7960
0.0440	332.97	0.4470
0.0800	332.97	0.5750
0.1250	332.97	0.6520
0.1630	332.97	0.6980
0.2020	332.97	0.7190
0.2440	332.97	0.7360
0.3060	332.97	0.7450
0.3760	332.97	0.7360
0.4350	332.97	0.7210
0.4950	332.97	0.7050

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Nitric oxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0730	292.97	1762.40
0.0940	292.97	2299.80
0.1300	292.97	3161.90
0.1530	292.97	3645.30
0.2040	292.97	4984.00
0.2780	292.97	6479.90
0.3520	292.97	8265.90
0.4010	292.97	9560.60
0.4450	292.97	10774.40
0.4950	292.97	12048.20
0.5720	292.97	13591.50
0.6750	292.97	14893.90
0.7300	292.97	15369.10
0.0330	312.93	1014.50
0.0780	312.93	2083.10
0.1260	312.93	3137.80
0.1750	312.93	4137.00
0.2290	312.93	5379.70
0.3080	312.93	6758.40
0.3600	312.93	8210.40
0.4200	312.93	9705.40
0.5070	312.93	11685.30
0.6360	312.93	13264.80
0.0440	332.97	1612.20
0.0800	332.97	2460.20
0.1250	332.97	3391.30
0.1630	332.97	4180.80
0.2020	332.97	5021.90
0.2440	332.97	6024.50
0.3060	332.97	7404.60
0.3760	332.97	8848.00
0.4350	332.97	9968.70
0.4950	332.97	10596.60

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Nitric oxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0730	292.97	1762.40
0.0940	292.97	2299.80
0.1300	292.97	3161.90
0.1530	292.97	3645.30
0.2040	292.97	4984.00
0.2780	292.97	6479.90
0.3520	292.97	8265.90
0.4010	292.97	9560.60
0.4450	292.97	10774.40
0.4950	292.97	12048.20
0.5720	292.97	13591.50
0.6750	292.97	14893.90
0.7300	292.97	15369.10
0.0330	312.93	1014.50
0.0780	312.93	2083.10
0.1260	312.93	3137.80
0.1750	312.93	4137.00
0.2290	312.93	5379.70
0.3080	312.93	6758.40
0.3600	312.93	8210.40
0.4200	312.93	9705.40
0.5070	312.93	11685.30
0.6360	312.93	13264.80
0.0440	332.97	1612.20
0.0800	332.97	2460.20
0.1250	332.97	3391.30
0.1630	332.97	4180.80
0.2020	332.97	5021.90
0.2440	332.97	6024.50
0.3060	332.97	7404.60
0.3760	332.97	8848.00
0.4350	332.97	9968.70
0.4950	332.97	10596.60

Sources

• Vapor Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K