Mixture of Heptane + Nonane

Datasets

1. Mole fraction (2)
2. P_c - Critical pressure, kPa (2)
3. T_boil - Boiling temperature at pressure P, K (2)
4. T_c - Critical temperature, K (2)

Mole fraction of Nonane (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Nonane (2) - Liquid	Mole fraction of Nonane (2) - Gas
0.0000	0.0000
0.0710	0.0100
0.1630	0.0270
0.2490	0.0500
0.3670	0.0840
0.4200	0.1170
0.5340	0.1760
0.6410	0.2740
0.7220	0.3750
0.8020	0.5060
0.8300	0.5600
0.8830	0.6750
0.9020	0.7200
0.9570	0.8670
0.9650	0.8910
1.0000	1.0000

Mole fraction of Nonane (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Nonane (2) - Liquid	Mole fraction of Nonane (2) - Gas
0.0000	0.0000
0.0710	0.0100
0.1630	0.0270
0.2490	0.0500
0.3670	0.0840
0.4200	0.1170
0.5340	0.1760
0.6410	0.2740
0.7220	0.3750
0.8020	0.5060
0.8300	0.5600
0.8830	0.6750
0.9020	0.7200
0.9570	0.8670
0.9650	0.8910
1.0000	1.0000

Critical pressure, kPa [ref]

Mole fraction of Heptane (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	2392.00
0.2000	2447.00
0.3000	2499.00
0.4000	2566.00
0.5000	2631.00
0.6000	2674.00
0.7000	2714.00
0.8000	2742.00
0.9000	2767.00

Critical pressure, kPa [ref]

Mole fraction of Heptane (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	2392.00
0.2000	2447.00
0.3000	2499.00
0.4000	2566.00
0.5000	2631.00
0.6000	2674.00
0.7000	2714.00
0.8000	2742.00
0.9000	2767.00

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Nonane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	371.40
0.0710	373.30
0.1630	375.70
0.2490	378.70
0.3670	382.30
0.4200	385.10
0.5340	390.30
0.6410	396.20
0.7220	401.60
0.8020	407.50
0.8300	409.60
0.8830	413.90
0.9020	415.50
0.9570	420.00
0.9650	420.70
1.0000	423.80

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Nonane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	371.40
0.0710	373.30
0.1630	375.70
0.2490	378.70
0.3670	382.30
0.4200	385.10
0.5340	390.30
0.6410	396.20
0.7220	401.60
0.8020	407.50
0.8300	409.60
0.8830	413.90
0.9020	415.50
0.9570	420.00
0.9650	420.70
1.0000	423.80

Critical temperature, K [ref]

Mole fraction of Heptane (1) - Liquid	Critical temperature, K - Liquid
0.1000	589.58
0.2000	585.47
0.3000	581.66
0.4000	576.80
0.5000	572.12
0.6000	567.30
0.7000	562.53
0.8000	556.49
0.9000	550.58

Critical temperature, K [ref]

Mole fraction of Heptane (1) - Liquid	Critical temperature, K - Liquid
0.1000	589.58
0.2000	585.47
0.3000	581.66
0.4000	576.80
0.5000	572.12
0.6000	567.30
0.7000	562.53
0.8000	556.49
0.9000	550.58

Sources

• Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus