Mixture of Tridecane + 2,3-Pentadione

Datasets

1. Liquid-liquid equilibrium temperature, K
2. P_vap - Vapor or sublimation pressure, kPa
3. T_fus - Solid-liquid equilibrium temperature, K

Liquid-liquid equilibrium temperature, K [ref]

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

Mole fraction of Tridecane (1) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.0897	264.87
0.1477	274.35
0.1826	280.24
0.2280	283.60
0.2439	285.19
0.3037	287.13
0.3432	287.52
0.3736	286.12
0.4089	283.53
0.4501	281.35
0.4880	278.21
0.5306	273.15
0.5700	267.07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tridecane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	293.15	697870.00
0.0000	303.15	807350.00
0.0000	313.15	947230.00
0.0000	323.15	1117520.00
0.0000	333.15	1318200.00
0.0000	343.15	1549280.00
0.0488	293.15	195790.00
0.0488	303.15	263250.00
0.0488	313.15	334070.00
0.0488	323.15	408260.00
0.0488	333.15	485810.00
0.0488	343.15	566720.00
0.0985	293.15	180670.00
0.0985	303.15	246930.00
0.0985	313.15	317220.00
0.0985	323.15	391540.00
0.0985	333.15	469870.00
0.0985	343.15	552240.00
0.1883	293.15	162290.00
0.1883	303.15	226320.00
0.1883	313.15	295190.00
0.1883	323.15	368900.00
0.1883	333.15	447440.00
0.1883	343.15	530830.00
0.2860	293.15	156980.00
0.2860	303.15	219970.00
0.2860	313.15	287880.00
0.2860	323.15	360700.00
0.2860	333.15	438450.00
0.2860	343.15	521110.00
0.3972	293.15	154340.00
0.3972	303.15	217040.00
0.3972	313.15	284500.00
0.3972	323.15	356700.00
0.3972	333.15	433660.00
0.3972	343.15	515370.00
0.4910	293.15	152520.00
0.4910	303.15	215380.00
0.4910	313.15	282760.00
0.4910	323.15	354670.00
0.4910	333.15	431120.00
0.4910	343.15	512100.00
0.5670	293.15	150530.00
0.5670	303.15	213870.00
0.5670	313.15	281520.00
0.5670	323.15	353470.00
0.5670	333.15	429730.00
0.5670	343.15	510290.00
0.6398	293.15	148280.00
0.6398	303.15	211880.00
0.6398	313.15	279710.00
0.6398	323.15	351740.00
0.6398	333.15	428000.00
0.6398	343.15	508470.00
0.6995	293.15	146460.00
0.6995	303.15	210070.00
0.6995	313.15	277920.00
0.6995	323.15	350010.00
0.6995	333.15	426340.00
0.6995	343.15	506910.00
0.7711	293.15	143630.00
0.7711	303.15	207690.00
0.7711	313.15	275860.00
0.7711	323.15	348140.00
0.7711	333.15	424520.00
0.7711	343.15	505010.00
0.8770	293.15	139440.00
0.8770	303.15	203560.00
0.8770	313.15	271850.00
0.8770	323.15	344320.00
0.8770	333.15	420970.00
0.8770	343.15	501790.00
0.9674	293.15	134840.00
0.9674	303.15	198700.00
0.9674	313.15	266980.00
0.9674	323.15	339710.00
0.9674	333.15	416870.00
0.9674	343.15	498460.00
1.0000	293.15	132350.00
1.0000	303.15	196230.00
1.0000	313.15	264630.00
1.0000	323.15	337550.00
1.0000	333.15	415000.00
1.0000	343.15	496960.00

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Tridecane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0105	255.26
0.0438	259.35
0.6022	264.12
0.6383	264.75
0.6761	265.39
0.7217	266.08
0.7639	266.48
0.8194	267.02
0.8769	267.57
0.9335	268.26
0.9828	268.80
1.0000	269.01

Sources

• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure

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