Mixture of Tridecane + 1-Hexyne

Datasets

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

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tridecane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
293.15	0.0312	505230.00
293.15	0.1007	393930.00
293.15	0.1798	334430.00
293.15	0.2589	274930.00
293.15	0.3403	247510.00
293.15	0.4196	226700.00
293.15	0.4994	206590.00
293.15	0.5616	199010.00
293.15	0.6587	184210.00
293.15	0.7391	170900.00
293.15	0.8084	162000.00
293.15	0.9001	149100.00
293.15	0.9791	138180.00
293.15	1.0000	133010.00
303.15	0.0312	599850.00
303.15	0.1007	486550.00
303.15	0.1798	423040.00
303.15	0.2589	359530.00
303.15	0.3403	330800.00
303.15	0.4196	311940.00
303.15	0.4994	284740.00
303.15	0.5616	270760.00
303.15	0.6587	254490.00
303.15	0.7391	241220.00
303.15	0.8084	229340.00
303.15	0.9001	218700.00
303.15	0.9791	205250.00
303.15	1.0000	197130.00
313.15	0.0312	688490.00
313.15	0.1007	574190.00
313.15	0.1798	509620.00
313.15	0.2589	445060.00
313.15	0.3403	419350.00
313.15	0.4196	394500.00
313.15	0.4994	367320.00
313.15	0.5616	349670.00
313.15	0.6587	329290.00
313.15	0.7391	315730.00
313.15	0.8084	299820.00
313.15	0.9001	290040.00
313.15	0.9791	276070.00
313.15	1.0000	265400.00
323.15	0.0312	776120.00
323.15	0.1007	656860.00
323.15	0.1798	594180.00
323.15	0.2589	531500.00
323.15	0.3403	513180.00
323.15	0.4196	482920.00
323.15	0.4994	454350.00
323.15	0.5616	435740.00
323.15	0.6587	408610.00
323.15	0.7391	394440.00
323.15	0.8084	376760.00
323.15	0.9001	363100.00
323.15	0.9791	350650.00
323.15	1.0000	337830.00
333.15	0.0312	863820.00
333.15	0.1007	734560.00
333.15	0.1798	676720.00
333.15	0.2589	618870.00
333.15	0.3403	599600.00
333.15	0.4196	577190.00
333.15	0.4994	545820.00
333.15	0.5616	528970.00
333.15	0.6587	492450.00
333.15	0.7391	477350.00
333.15	0.8084	460160.00
333.15	0.9001	437900.00
333.15	0.9791	428980.00
333.15	1.0000	414420.00
343.15	0.0312	969260.00
343.15	0.1007	825000.00
343.15	0.1798	786500.00
343.15	0.2589	748000.00
343.15	0.3403	707000.00
343.15	0.4196	677320.00
343.15	0.4994	641730.00
343.15	0.5616	620900.00
343.15	0.6587	580810.00
343.15	0.7391	564450.00
343.15	0.8084	550030.00
343.15	0.9001	514420.00
343.15	0.9791	498100.00
343.15	1.0000	495180.00

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Tridecane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.4103	255.32
0.4282	255.78
0.4480	256.65
0.4714	257.43
0.5056	258.44
0.5451	259.37
0.5745	260.06
0.6053	260.95
0.6397	262.05
0.6663	262.72
0.6957	263.31
0.7338	264.45
0.7731	265.30
0.8093	266.00
0.8372	266.74
0.8774	267.47
0.9203	268.13
0.9697	268.81
1.0000	269.01

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Tridecane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0035	231.94
0.0665	240.75
0.1057	245.25
0.1473	247.76
0.1744	248.79
0.1981	249.62
0.2314	250.91
0.2593	251.64
0.2904	252.69
0.3058	253.15
0.3321	253.55
0.3457	253.77
0.3556	253.81
0.3702	254.12
0.3828	254.37

Sources

• Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction

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