Mixture of Benzene + Acetone + Methyl Alcohol

Datasets

1. Binary diffusion coefficient, m2/s (2)
2. Vapor Liquid Equilibrium at Constant Pressure

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)
• Mole fraction = 0 (Liquid)

Solvent: Mole fraction of Acetone (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.1220	0.0000
0.2099	0.0000
0.3594	0.0000
0.5372	0.0000
0.7061	0.0000
0.7900	0.0000
0.8781	0.0000
1.0000	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)
• Mole fraction = 0 (Liquid)

Solvent: Mole fraction of Acetone (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.1220	0.0000
0.2099	0.0000
0.3594	0.0000
0.5372	0.0000
0.7061	0.0000
0.7900	0.0000
0.8781	0.0000
1.0000	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.3 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetone (2) - Liquid	x2[mol/mol] of Methyl Alcohol (3) - Liquid	y1[mol/mol] of Acetone (2) - Vapour	y2[mol/mol] of Methyl Alcohol (3) - Vapour
353.24	0.0000	0.0000	0.0000	0.0000
337.7	0.0000	1.0000	0.0000	1.0000
329.26	1.0000	0.0000	1.0000	0.0000
331.14	0.0230	0.5110	0.0230	0.5840
333.6	0.0240	0.9040	0.0410	0.7840
332.27	0.0600	0.8310	0.0910	0.7030
335.04	0.0660	0.1030	0.0910	0.4190
333.28	0.0660	0.8760	0.1130	0.7550
330.87	0.0940	0.6230	0.1080	0.5850
332.54	0.1180	0.2100	0.1320	0.4560
330.73	0.1360	0.5330	0.1480	0.5430
333.95	0.1460	0.1330	0.1820	0.3870
331.2	0.1490	0.7270	0.1990	0.6160
330.65	0.1540	0.5840	0.1740	0.5530
330.6	0.1750	0.5080	0.1910	0.5210
330.71	0.1910	0.4340	0.2030	0.4940
330.45	0.2010	0.5460	0.2250	0.5240
331.65	0.2090	0.2570	0.2250	0.4270
331.36	0.2140	0.7350	0.3040	0.6120
330.72	0.2180	0.6680	0.2780	0.5690
332.96	0.2190	0.1640	0.2550	0.3680
330.35	0.2290	0.5690	0.2640	0.5220
333.23	0.2500	0.1420	0.2960	0.3330
330.34	0.2540	0.4590	0.2720	0.4770
334.78	0.2740	0.0850	0.3570	0.2490
330.18	0.2740	0.5550	0.3140	0.5030
330.34	0.2750	0.6190	0.3370	0.5320
330.13	0.2970	0.4570	0.3210	0.4610
330.67	0.3100	0.3160	0.3230	0.4070
331.71	0.3200	0.2040	0.3480	0.3450
330.04	0.3230	0.5780	0.3860	0.4990
329.98	0.3270	0.4680	0.3550	0.4560
329.82	0.3500	0.4990	0.3890	0.4600
334.41	0.3510	0.0770	0.4440	0.2010
329.92	0.3610	0.4150	0.3830	0.4250
330.05	0.3720	0.3780	0.3910	0.4050
329.97	0.3980	0.3520	0.4160	0.3880
329.64	0.4000	0.5130	0.4550	0.4520
330.89	0.4050	0.2240	0.4280	0.3280
329.61	0.4130	0.4340	0.4420	0.4170
333.93	0.4260	0.0670	0.5230	0.1600
329.61	0.4390	0.3800	0.4610	0.3870
330.81	0.4470	0.2070	0.4720	0.3010
334.48	0.4670	0.0410	0.5910	0.1000
329.35	0.4780	0.3950	0.5060	0.3820
330.72	0.4890	0.1920	0.5140	0.2760
329.47	0.4920	0.3420	0.5110	0.3550
334.16	0.4980	0.0380	0.6200	0.0890
329.79	0.5040	0.2750	0.5180	0.3190
329.18	0.5080	0.4200	0.5480	0.3840
331.07	0.5230	0.1480	0.5590	0.2280
331.73	0.5320	0.1080	0.5860	0.1860
329.69	0.5370	0.2610	0.5500	0.3020
333.66	0.5530	0.0330	0.6690	0.0700
329.66	0.5620	0.2450	0.5730	0.2870
330.5	0.5790	0.1560	0.6050	0.2190
328.98	0.5870	0.3310	0.6070	0.3240
328.82	0.6100	0.3510	0.6370	0.3280
328.96	0.6170	0.2970	0.6310	0.3000
330.4	0.6210	0.1400	0.6460	0.1960
328.96	0.6460	0.2630	0.6560	0.2740
330.31	0.6580	0.1250	0.6810	0.1760
328.66	0.6690	0.2920	0.6820	0.2860
329.01	0.6820	0.2220	0.6860	0.2430
330.2	0.7070	0.1050	0.7300	0.1470
328.6	0.7280	0.2400	0.7310	0.2440
328.6	0.7500	0.2200	0.7490	0.2280
329.47	0.7650	0.1220	0.7700	0.1530
329.21	0.8160	0.1100	0.8170	0.1320
329.24	0.8440	0.0920	0.8440	0.1120

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods