Mixture of Tetrachloroethylene + Tetrahydrofuran

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrachloroethylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
283.15	0.0556	10.22
283.15	0.1845	9.00
283.15	0.2713	8.20
283.15	0.3291	7.67
283.15	0.3890	7.11
283.15	0.5024	6.07
283.15	0.5770	5.38
283.15	0.6789	4.39
283.15	0.7742	3.46
283.15	0.8579	2.59
283.15	0.8871	2.28
283.15	0.9339	1.78
288.15	0.0556	13.00
288.15	0.1846	11.49
288.15	0.2714	10.46
288.15	0.3293	9.81
288.15	0.3892	9.09
288.15	0.5025	7.79
288.15	0.5772	6.93
288.15	0.6790	5.67
288.15	0.7742	4.50
288.15	0.8580	3.38
288.15	0.8872	3.00
288.15	0.9339	2.35
293.15	0.0556	16.40
293.15	0.1848	14.48
293.15	0.2715	13.21
293.15	0.3296	12.40
293.15	0.3895	11.50
293.15	0.5026	9.86
293.15	0.5774	8.79
293.15	0.6791	7.25
293.15	0.7743	5.74
293.15	0.8580	4.35
293.15	0.8872	3.85
293.15	0.9340	3.05
298.15	0.0556	20.56
298.15	0.1846	18.18
298.15	0.2717	16.60
298.15	0.3300	15.55
298.15	0.3902	14.47
298.15	0.5028	12.45
298.15	0.5777	11.08
298.15	0.6793	9.16
298.15	0.7745	7.29
298.15	0.8581	5.56
298.15	0.8873	4.93
298.15	0.9340	3.92
303.15	0.0556	25.52
303.15	0.1847	22.61
303.15	0.2715	20.66
303.15	0.3295	19.44
303.15	0.3895	18.05
303.15	0.5031	15.52
303.15	0.5782	13.86
303.15	0.6796	11.46
303.15	0.7747	9.17
303.15	0.8583	7.02
303.15	0.8874	6.27
303.15	0.9341	5.02
308.15	0.0557	31.38
308.15	0.1848	27.78
308.15	0.2717	25.41
308.15	0.3300	23.85
308.15	0.3901	22.23
308.15	0.5026	19.20
308.15	0.5775	17.16
308.15	0.6793	14.25
308.15	0.7749	11.40
308.15	0.8585	8.80
308.15	0.8875	7.87
308.15	0.9342	6.34
313.15	0.0557	38.29
313.15	0.1849	33.99
313.15	0.2718	31.09
313.15	0.3302	29.20
313.15	0.3902	27.20
313.15	0.5029	23.49
313.15	0.5780	21.05
313.15	0.6795	17.55
313.15	0.7754	14.11
313.15	0.8587	10.96
313.15	0.8876	9.83
313.15	0.9343	7.95
318.15	0.0558	46.36
318.15	0.1851	41.17
318.15	0.2721	37.67
318.15	0.3307	35.46
318.15	0.3913	33.02
318.15	0.5033	28.59
318.15	0.5783	25.64
318.15	0.6797	21.46
318.15	0.7749	17.27
318.15	0.8591	13.49
318.15	0.8879	12.09
318.15	0.9344	9.87
323.15	0.0559	55.81
323.15	0.1854	49.54
323.15	0.2727	45.42
323.15	0.3307	42.75
323.15	0.3915	39.84
323.15	0.5032	34.52
323.15	0.5786	30.97
323.15	0.6803	25.94
323.15	0.7751	21.06
323.15	0.8595	16.50
323.15	0.8881	14.83
323.15	0.9346	12.17

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrachloroethylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
283.15	0.0556	10.22
283.15	0.1845	9.00
283.15	0.2713	8.20
283.15	0.3291	7.67
283.15	0.3890	7.11
283.15	0.5024	6.07
283.15	0.5770	5.38
283.15	0.6789	4.39
283.15	0.7742	3.46
283.15	0.8579	2.59
283.15	0.8871	2.28
283.15	0.9339	1.78
288.15	0.0556	13.00
288.15	0.1846	11.49
288.15	0.2714	10.46
288.15	0.3293	9.81
288.15	0.3892	9.09
288.15	0.5025	7.79
288.15	0.5772	6.93
288.15	0.6790	5.67
288.15	0.7742	4.50
288.15	0.8580	3.38
288.15	0.8872	3.00
288.15	0.9339	2.35
293.15	0.0556	16.40
293.15	0.1848	14.48
293.15	0.2715	13.21
293.15	0.3296	12.40
293.15	0.3895	11.50
293.15	0.5026	9.86
293.15	0.5774	8.79
293.15	0.6791	7.25
293.15	0.7743	5.74
293.15	0.8580	4.35
293.15	0.8872	3.85
293.15	0.9340	3.05
298.15	0.0556	20.56
298.15	0.1846	18.18
298.15	0.2717	16.60
298.15	0.3300	15.55
298.15	0.3902	14.47
298.15	0.5028	12.45
298.15	0.5777	11.08
298.15	0.6793	9.16
298.15	0.7745	7.29
298.15	0.8581	5.56
298.15	0.8873	4.93
298.15	0.9340	3.92
303.15	0.0556	25.52
303.15	0.1847	22.61
303.15	0.2715	20.66
303.15	0.3295	19.44
303.15	0.3895	18.05
303.15	0.5031	15.52
303.15	0.5782	13.86
303.15	0.6796	11.46
303.15	0.7747	9.17
303.15	0.8583	7.02
303.15	0.8874	6.27
303.15	0.9341	5.02
308.15	0.0557	31.38
308.15	0.1848	27.78
308.15	0.2717	25.41
308.15	0.3300	23.85
308.15	0.3901	22.23
308.15	0.5026	19.20
308.15	0.5775	17.16
308.15	0.6793	14.25
308.15	0.7749	11.40
308.15	0.8585	8.80
308.15	0.8875	7.87
308.15	0.9342	6.34
313.15	0.0557	38.29
313.15	0.1849	33.99
313.15	0.2718	31.09
313.15	0.3302	29.20
313.15	0.3902	27.20
313.15	0.5029	23.49
313.15	0.5780	21.05
313.15	0.6795	17.55
313.15	0.7754	14.11
313.15	0.8587	10.96
313.15	0.8876	9.83
313.15	0.9343	7.95
318.15	0.0558	46.36
318.15	0.1851	41.17
318.15	0.2721	37.67
318.15	0.3307	35.46
318.15	0.3913	33.02
318.15	0.5033	28.59
318.15	0.5783	25.64
318.15	0.6797	21.46
318.15	0.7749	17.27
318.15	0.8591	13.49
318.15	0.8879	12.09
318.15	0.9344	9.87
323.15	0.0559	55.81
323.15	0.1854	49.54
323.15	0.2727	45.42
323.15	0.3307	42.75
323.15	0.3915	39.84
323.15	0.5032	34.52
323.15	0.5786	30.97
323.15	0.6803	25.94
323.15	0.7751	21.06
323.15	0.8595	16.50
323.15	0.8881	14.83
323.15	0.9346	12.17

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	392.25
0.1521	378.65
0.2650	370.25
0.3570	364.15
0.4741	357.45
0.5955	351.55
0.6883	347.65
0.8154	342.95
1.0000	337.55

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	392.25
0.1521	378.65
0.2650	370.25
0.3570	364.15
0.4741	357.45
0.5955	351.55
0.6883	347.65
0.8154	342.95
1.0000	337.55

Sources

• Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa