Mixture of 1-Hexene + 2-Propanol

Datasets

1. P_vap - Vapor or sublimation pressure, kPa
2. Vapor Liquid Equilibrium at Constant Pressure
3. Vapor Liquid Equilibrium at Constant Temperature

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Hexene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
293.18	0.0000	4.20
293.18	0.0558	9.40
293.18	0.1018	12.30
293.18	0.1490	14.50
293.18	0.2011	16.30
293.18	0.2551	17.60
293.18	0.3029	18.40
293.18	0.3542	19.10
293.18	0.4000	19.60
293.18	0.4499	20.10
293.18	0.4998	20.30
293.18	0.5521	20.60
293.18	0.5999	20.80
293.18	0.6488	21.00
293.18	0.7008	21.10
293.18	0.7421	21.20
293.18	0.8025	21.40
293.18	0.8525	21.50
293.18	0.9044	21.50
293.18	0.9319	21.40
293.18	1.0000	20.00
303.16	0.0000	7.90
303.16	0.0563	15.50
303.16	0.1007	19.70
303.16	0.1563	23.40
303.16	0.2025	25.70
303.16	0.2536	27.50
303.16	0.3014	28.80
303.16	0.3541	29.80
303.16	0.4021	30.60
303.17	0.4519	31.50
303.16	0.5006	31.70
303.17	0.5495	32.10
303.17	0.5976	32.40
303.17	0.6504	32.70
303.17	0.7020	32.90
303.17	0.7490	33.10
303.17	0.7966	33.20
303.17	0.8489	33.30
303.17	0.9004	33.30
303.17	0.9460	33.00
303.17	1.0000	30.60
313.16	0.0000	14.00
313.16	0.0481	23.40
313.16	0.1044	30.90
313.16	0.1551	35.70
313.16	0.1952	38.50
313.16	0.2503	41.40
313.16	0.3044	43.50
313.16	0.3537	44.90
313.16	0.4034	46.00
313.16	0.4507	46.90
313.16	0.4681	47.20
313.16	0.5040	47.70
313.16	0.5512	48.20
313.16	0.5999	48.70
313.16	0.6539	49.20
313.16	0.6963	49.50
313.16	0.7463	49.70
313.16	0.7952	49.90
313.16	0.8505	50.00
313.16	0.8964	49.80
313.16	0.9517	49.10
313.16	1.0000	45.10

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.3 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid	y1[mol/mol] of 1-Hexene (1) - Vapour
355.51	0.0000	0.0000
350.95	0.0240	0.1260
345.7	0.0770	0.3210
344.39	0.0920	0.3640
343.92	0.1050	0.3780
339.71	0.1820	0.5130
338.32	0.2090	0.5490
337.09	0.2610	0.5780
335.71	0.3100	0.6190
335.0	0.3610	0.6430
334.41	0.4100	0.6670
333.96	0.4450	0.6890
333.28	0.5060	0.6910
332.76	0.5940	0.7270
332.56	0.6530	0.7480
332.53	0.6570	0.7370
332.51	0.7460	0.7690
332.38	0.7520	0.7750
331.77	0.7760	0.7850
331.58	0.7980	0.7930
332.44	0.8390	0.8150
332.49	0.8730	0.8430
336.65	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

x1[mol/mol] of 1-Hexene (1) - Liquid	y1[mol/mol] of 1-Hexene (1) - Vapour
0.1000	0.5130
0.2010	0.6070
0.3430	0.6600
0.4000	0.6730
0.5980	0.7440
0.8000	0.8170
0.9000	0.8660

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol

Note: These property values are available through the Cheméo API. A free account gives you an access key.