Mixture of Nitrous oxide + Methyl fluoride

Datasets

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

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 182.33 (Liquid)

Mole fraction of Methyl fluoride (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1556	83.62
0.3199	77.48
0.3984	74.65
0.4074	74.59
0.5454	68.94
0.5586	67.78
0.6708	63.12
0.7053	61.73
0.7968	57.57
0.8128	56.77
0.8878	53.45
0.8898	53.06

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 182.33 (Liquid)

Mole fraction of Methyl fluoride (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1556	83.62
0.3199	77.48
0.3984	74.65
0.4074	74.59
0.5454	68.94
0.5586	67.78
0.6708	63.12
0.7053	61.73
0.7968	57.57
0.8128	56.77
0.8878	53.45
0.8898	53.06

Molar volume, m3/mol [ref]

Fixed			Measured
Mole fraction of Nitrous oxide (1) - Fluid (supercritical or subcritical phases)	Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Molar volume, m3/mol - Fluid (supercritical or subcritical phases)
0.1467	273.05	1878.40	0.0009
0.1467	282.83	1994.70	0.0009
0.1467	292.79	2109.40	0.0009
0.1467	298.08	2168.40	0.0009
0.1467	308.05	2279.30	0.0009
0.1467	318.05	2388.70	0.0009
0.1467	328.03	2496.30	0.0009
0.1467	338.09	2603.10	0.0009
0.1467	347.94	2707.00	0.0009
0.1467	354.94	2779.90	0.0009
0.3047	268.00	2048.20	0.0007
0.3047	273.01	2223.50	0.0007
0.3047	282.81	2371.80	0.0007
0.3047	292.96	2512.20	0.0007
0.3047	298.17	2591.90	0.0007
0.3047	308.13	2731.20	0.0007
0.3047	318.11	2867.70	0.0007
0.3047	328.10	3002.90	0.0007
0.3047	338.09	3135.80	0.0007
0.3047	348.06	3267.00	0.0007
0.3047	358.03	3396.50	0.0007
0.5080	263.03	1936.10	0.0009
0.5080	267.98	1999.20	0.0009
0.5080	272.89	2060.30	0.0009
0.5080	277.86	2121.00	0.0009
0.5080	288.08	2242.80	0.0009
0.5080	298.09	2358.50	0.0009
0.5080	308.06	2474.50	0.0009
0.5080	318.12	2588.20	0.0009
0.5080	328.11	2699.90	0.0009
0.5080	338.08	2810.20	0.0009
0.5080	348.06	2919.80	0.0009
0.5080	358.05	3028.80	0.0009
0.6161	263.02	2088.50	0.0008
0.6161	268.00	2223.90	0.0008
0.6161	272.98	2295.80	0.0008
0.6161	283.04	2438.00	0.0008
0.6161	293.07	2574.60	0.0008
0.6161	298.11	2642.60	0.0008
0.6161	308.15	2774.90	0.0008
0.6161	318.12	2904.60	0.0008
0.6161	328.09	3033.00	0.0008
0.6161	338.08	3160.00	0.0008
0.6161	348.05	3285.80	0.0008
0.6161	358.03	3410.50	0.0008
0.8263	287.80	4359.80	0.0003
0.8263	292.93	4761.60	0.0003
0.8263	302.97	5179.00	0.0003
0.8263	307.96	5380.90	0.0003
0.8263	312.91	5577.90	0.0003

Molar volume, m3/mol [ref]

Fixed			Measured
Mole fraction of Nitrous oxide (1) - Fluid (supercritical or subcritical phases)	Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Molar volume, m3/mol - Fluid (supercritical or subcritical phases)
0.1467	273.05	1878.40	0.0009
0.1467	282.83	1994.70	0.0009
0.1467	292.79	2109.40	0.0009
0.1467	298.08	2168.40	0.0009
0.1467	308.05	2279.30	0.0009
0.1467	318.05	2388.70	0.0009
0.1467	328.03	2496.30	0.0009
0.1467	338.09	2603.10	0.0009
0.1467	347.94	2707.00	0.0009
0.1467	354.94	2779.90	0.0009
0.3047	268.00	2048.20	0.0007
0.3047	273.01	2223.50	0.0007
0.3047	282.81	2371.80	0.0007
0.3047	292.96	2512.20	0.0007
0.3047	298.17	2591.90	0.0007
0.3047	308.13	2731.20	0.0007
0.3047	318.11	2867.70	0.0007
0.3047	328.10	3002.90	0.0007
0.3047	338.09	3135.80	0.0007
0.3047	348.06	3267.00	0.0007
0.3047	358.03	3396.50	0.0007
0.5080	263.03	1936.10	0.0009
0.5080	267.98	1999.20	0.0009
0.5080	272.89	2060.30	0.0009
0.5080	277.86	2121.00	0.0009
0.5080	288.08	2242.80	0.0009
0.5080	298.09	2358.50	0.0009
0.5080	308.06	2474.50	0.0009
0.5080	318.12	2588.20	0.0009
0.5080	328.11	2699.90	0.0009
0.5080	338.08	2810.20	0.0009
0.5080	348.06	2919.80	0.0009
0.5080	358.05	3028.80	0.0009
0.6161	263.02	2088.50	0.0008
0.6161	268.00	2223.90	0.0008
0.6161	272.98	2295.80	0.0008
0.6161	283.04	2438.00	0.0008
0.6161	293.07	2574.60	0.0008
0.6161	298.11	2642.60	0.0008
0.6161	308.15	2774.90	0.0008
0.6161	318.12	2904.60	0.0008
0.6161	328.09	3033.00	0.0008
0.6161	338.08	3160.00	0.0008
0.6161	348.05	3285.80	0.0008
0.6161	358.03	3410.50	0.0008
0.8263	287.80	4359.80	0.0003
0.8263	292.93	4761.60	0.0003
0.8263	302.97	5179.00	0.0003
0.8263	307.96	5380.90	0.0003
0.8263	312.91	5577.90	0.0003

Sources

• PVTx measurements for N2O+CH3F, N2O+CH2F2, and N2O+ CHF3 binary systems
• Vapour pressure and excess Gibbs free energy of the ternary system {x1CH3F + x2HCl + x3N2O} at temperature of 182.33 K