Mixture of Heptane + Methyl Alcohol

Datasets

1. Mole fraction (20)
2. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
101.30	298.15	0.1520

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
298.15	101.30	0.8990

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
308.41	0.8870
312.96	0.8670
317.98	0.8440

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
308.41	0.2440
312.96	0.2890
317.98	0.3390

Mass fraction of Heptane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Heptane (1) - Liquid mixture 1
293.95	0.9494
293.95	0.9506
295.15	0.9476
295.15	0.9466
295.15	0.9468
295.15	0.9469
295.15	0.9465

Mass fraction of Heptane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Heptane (1) - Liquid mixture 2
293.95	0.2401
293.95	0.2391
295.15	0.2465
295.15	0.2465
295.15	0.2406
295.15	0.2408
295.15	0.2396

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0000	0.0000
0.2470	0.7370
0.3490	0.7380
0.3990	0.7400
0.5010	0.7430
0.5740	0.7470
0.6290	0.7490
0.6720	0.7500
0.7070	0.7670
0.7350	0.7750
0.7490	0.7750
0.7580	0.7750
0.7740	0.7770
0.7780	0.7790
0.8020	0.7810
0.8300	0.7830
0.8610	0.7860
0.8940	0.7950
0.9110	0.8000
0.9290	0.8180
0.9580	0.8240
1.0000	1.0000

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0258	0.5465
0.0524	0.6714
0.0716	0.6917
0.0972	0.7067
0.1493	0.7085
0.2017	0.7207
0.2595	0.7355
0.2984	0.7318
0.3479	0.7362
0.3983	0.7401
0.4531	0.7373
0.5000	0.7403
0.5508	0.7275
0.6002	0.7423
0.6498	0.7478
0.7013	0.7515
0.7504	0.7436
0.8003	0.7486
0.8500	0.7556
0.9002	0.7712
0.9252	0.7878
0.9499	0.8396
0.9797	0.9087

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
268.15	0.0760
278.15	0.0950
288.15	0.1270
298.15	0.1530

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
268.15	0.9530
278.15	0.9360
288.15	0.9150
298.15	0.9040

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
101.30	298.15	0.1520

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
298.15	101.30	0.8990

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
308.41	0.8870
312.96	0.8670
317.98	0.8440

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
308.41	0.2440
312.96	0.2890
317.98	0.3390

Mass fraction of Heptane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Heptane (1) - Liquid mixture 1
293.95	0.9494
293.95	0.9506
295.15	0.9476
295.15	0.9466
295.15	0.9468
295.15	0.9469
295.15	0.9465

Mass fraction of Heptane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Heptane (1) - Liquid mixture 2
293.95	0.2401
293.95	0.2391
295.15	0.2465
295.15	0.2465
295.15	0.2406
295.15	0.2408
295.15	0.2396

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0000	0.0000
0.2470	0.7370
0.3490	0.7380
0.3990	0.7400
0.5010	0.7430
0.5740	0.7470
0.6290	0.7490
0.6720	0.7500
0.7070	0.7670
0.7350	0.7750
0.7490	0.7750
0.7580	0.7750
0.7740	0.7770
0.7780	0.7790
0.8020	0.7810
0.8300	0.7830
0.8610	0.7860
0.8940	0.7950
0.9110	0.8000
0.9290	0.8180
0.9580	0.8240
1.0000	1.0000

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0258	0.5465
0.0524	0.6714
0.0716	0.6917
0.0972	0.7067
0.1493	0.7085
0.2017	0.7207
0.2595	0.7355
0.2984	0.7318
0.3479	0.7362
0.3983	0.7401
0.4531	0.7373
0.5000	0.7403
0.5508	0.7275
0.6002	0.7423
0.6498	0.7478
0.7013	0.7515
0.7504	0.7436
0.8003	0.7486
0.8500	0.7556
0.9002	0.7712
0.9252	0.7878
0.9499	0.8396
0.9797	0.9087

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
268.15	0.0760
278.15	0.0950
288.15	0.1270
298.15	0.1530

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 2
268.15	0.9530
278.15	0.9360
288.15	0.9150
298.15	0.9040

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	365.65
0.2470	331.55
0.3490	330.85
0.3990	329.95
0.5010	329.65
0.5740	329.55
0.6290	329.25
0.6720	329.25
0.7070	328.95
0.7350	328.25
0.7490	327.55
0.7580	328.45
0.7740	327.45
0.7780	327.45
0.8020	327.35
0.8300	327.45
0.8610	327.55
0.8940	327.65
0.9110	327.75
0.9290	327.85
0.9580	328.65
1.0000	333.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	365.65
0.2470	331.55
0.3490	330.85
0.3990	329.95
0.5010	329.65
0.5740	329.55
0.6290	329.25
0.6720	329.25
0.7070	328.95
0.7350	328.25
0.7490	327.55
0.7580	328.45
0.7740	327.45
0.7780	327.45
0.8020	327.35
0.8300	327.45
0.8610	327.55
0.8940	327.65
0.9110	327.75
0.9290	327.85
0.9580	328.65
1.0000	333.15

Sources

• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + methanol + heptane
• A novel static analytical apparatus for phase equilibrium measurements
• Liquid-liquid equilibria of n-heptane, methanol and deep eutectic solvents composed of carboxylic acid and monocyclic terpenes
• Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
• Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
• Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane