Mixture of Benzene + Cyclohexane + Methyl Alcohol

Datasets

1. Vapor Liquid Equilibrium at Constant Pressure
2. Vapor Liquid Equilibrium at Constant Temperature (2)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (3) - Liquid	x2[mol/mol] of Benzene (1) - Liquid	y1[mol/mol] of Methyl Alcohol (3) - Vapour	y2[mol/mol] of Benzene (1) - Vapour
337.72	1.0000	0.0000	1.0000	0.0000
353.26	0.0000	1.0000	0.0000	1.0000
353.81	0.0000	0.0000	0.0000	0.0000
332.1	0.9170	0.0630	0.7780	0.1300
329.9	0.8360	0.1250	0.6560	0.2130
330.1	0.7640	0.1980	0.6380	0.2670
329.95	0.6940	0.2730	0.6100	0.3100
330.05	0.6060	0.3540	0.5730	0.3270
330.05	0.5190	0.4340	0.5830	0.3460
330.3	0.4270	0.5200	0.5790	0.3590
332.85	0.1160	0.2500	0.4940	0.1550
327.85	0.1940	0.2380	0.5520	0.1350
327.75	0.2660	0.2280	0.5610	0.1280
327.75	0.3800	0.2140	0.5650	0.1400
327.95	0.4600	0.2060	0.5590	0.1490
327.95	0.5320	0.1900	0.5620	0.1510
327.95	0.5970	0.1760	0.5700	0.1560
327.95	0.6510	0.1600	0.5640	0.1570
328.15	0.7070	0.1460	0.5780	0.1640
328.2	0.7370	0.1290	0.6080	0.1540
328.3	0.7640	0.1150	0.6160	0.1460
328.4	0.8130	0.0840	0.6150	0.1180
328.55	0.7360	0.1610	0.5990	0.1940
328.95	0.6500	0.2470	0.5770	0.2480
329.25	0.5740	0.3230	0.5690	0.2780
329.5	0.4890	0.4000	0.5820	0.2790
329.85	0.3900	0.4830	0.5600	0.3170
330.35	0.3010	0.5590	0.5430	0.3340
330.65	0.3070	0.5840	0.5410	0.3600
330.65	0.3020	0.6200	0.5460	0.3710
332.25	0.2500	0.7000	0.5280	0.4120
334.95	0.1480	0.7940	0.4820	0.4650
334.95	0.1120	0.5340	0.4150	0.3320
328.85	0.1390	0.2430	0.5480	0.1400
328.15	0.1660	0.2100	0.5490	0.1190
328.85	0.1420	0.2400	0.5540	0.1320
328.25	0.2720	0.3190	0.5510	0.1900
328.05	0.2610	0.2930	0.5490	0.1710
328.15	0.3560	0.2750	0.5560	0.1770
328.05	0.4650	0.2400	0.5530	0.1720
328.05	0.5300	0.2250	0.5610	0.1780
328.45	0.5310	0.2650	0.5580	0.2140
328.85	0.4810	0.3420	0.5540	0.2570
329.25	0.4110	0.4210	0.5460	0.2830
329.45	0.3310	0.4940	0.5440	0.3020
330.05	0.2400	0.6080	0.5310	0.3430
333.65	0.1670	0.6860	0.4780	0.4050
336.45	0.1010	0.7740	0.4250	0.4700
330.1	0.1600	0.4370	0.5110	0.2430
328.45	0.2940	0.3820	0.5450	0.2210
328.5	0.4040	0.3390	0.5480	0.2240
329.05	0.3220	0.4460	0.5410	0.2690
329.95	0.2210	0.5530	0.5420	0.2970
334.45	0.1470	0.6290	0.4430	0.3820
329.85	0.1500	0.5280	0.4720	0.3150
328.85	0.1830	0.4270	0.5260	0.2280
329.05	0.2730	0.4570	0.5350	0.2640
351.25	0.0130	0.9490	0.0240	0.9240
351.51	0.0090	0.8970	0.0040	0.8720
348.82	0.0160	0.8150	0.0800	0.7370
347.4	0.0140	0.6010	0.0760	0.5460
341.39	0.0270	0.5060	0.2210	0.3990
341.95	0.0160	0.4310	0.2070	0.3400
343.35	0.0050	0.3680	0.1780	0.3190
344.5	0.0100	0.3000	0.1700	0.2650
340.58	0.0180	0.2610	0.2750	0.2160
344.4	0.0210	0.6750	0.1650	0.5480
334.15	0.0900	0.4530	0.4340	0.2810
333.05	0.0840	0.3850	0.4730	0.2280
332.0	0.0800	0.3200	0.5040	0.1870
335.35	0.0610	0.5920	0.3940	0.3660

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 311.65 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (3) - Liquid	x2[mol/mol] of Benzene (1) - Liquid	y1[mol/mol] of Methyl Alcohol (3) - Vapour	y2[mol/mol] of Benzene (1) - Vapour
49.463	0.1000	0.2000	0.5000	0.1280
47.996	0.1000	0.4000	0.4690	0.2330
46.929	0.1000	0.5000	0.4570	0.2930
44.53	0.1000	0.7000	0.4520	0.3940
51.596	0.2000	0.2000	0.5260	0.1260
50.263	0.2000	0.4000	0.5050	0.2310
47.996	0.2000	0.6000	0.5020	0.3400
52.529	0.4000	0.2000	0.5350	0.1440
49.996	0.4000	0.4000	0.5190	0.2810
52.262	0.6000	0.2000	0.5410	0.1890

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (3) - Liquid	x2[mol/mol] of Benzene (1) - Liquid	y1[mol/mol] of Methyl Alcohol (3) - Vapour	y2[mol/mol] of Benzene (1) - Vapour
95.459	0.1000	0.2000	0.5260	0.1180
91.192	0.1000	0.4000	0.4890	0.2240
89.993	0.1000	0.5000	0.4790	0.2800
85.06	0.1000	0.7000	0.4750	0.3800
100.392	0.2000	0.2000	0.5550	0.1180
97.325	0.2000	0.4000	0.5440	0.2130
92.659	0.2000	0.6000	0.5200	0.3280
101.725	0.4000	0.2000	0.5530	0.1390
97.325	0.4000	0.4000	0.5570	0.2590

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data