Mixture of 1-Butanol + Acetone

Datasets

1. Mole fraction
2. Binary diffusion coefficient, m2/s (2)
3. Vapor Liquid Equilibrium at Constant Pressure (2)
4. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Acetone (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetone (2) - Liquid	Mole fraction of Acetone (2) - Gas
283.20	0.0120	0.6450
283.20	0.0370	0.8430
283.20	0.0870	0.9210
283.20	0.2910	0.9690
283.20	0.5520	0.9860
283.20	0.8260	0.9970
295.20	0.0120	0.4990
295.20	0.0370	0.7650
295.20	0.0870	0.8680
295.20	0.2910	0.9480
295.20	0.5520	0.9760
295.20	0.8260	0.9910
308.20	0.0120	0.4020
308.20	0.0370	0.6660
308.20	0.0870	0.8180
308.20	0.2910	0.9240
308.20	0.5520	0.9740
308.20	0.8260	0.9880
324.20	0.0120	0.2600
324.20	0.0370	0.5220
324.20	0.0870	0.7070
324.20	0.2910	0.8920
324.20	0.5520	0.9500
324.20	0.8260	0.9850

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Mole fraction of Acetone (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0125	0.0000
0.1000	0.0000
0.2000	0.0000
0.3000	0.0000
0.4000	0.0000
0.5000	0.0000
0.6000	0.0000
0.7000	0.0000
0.8000	0.0000
0.9000	0.0000
0.9915	0.0000
0.9925	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Mole fraction of Acetone (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0125	0.0000
0.1000	0.0000
0.2000	0.0000
0.3000	0.0000
0.4000	0.0000
0.5000	0.0000
0.6000	0.0000
0.7000	0.0000
0.8000	0.0000
0.9000	0.0000
0.9915	0.0000
0.9925	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 99.46 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetone (2) - Liquid	y1[mol/mol] of Acetone (2) - Vapour
388.15	0.0100	0.1050
385.15	0.0250	0.2250
380.25	0.0500	0.4050
376.95	0.0700	0.4720
364.85	0.1540	0.6980
360.05	0.1980	0.7500
358.55	0.2150	0.7730
354.85	0.2650	0.8090
351.95	0.3120	0.8370
341.75	0.5350	0.9300
339.35	0.6070	0.9430
337.65	0.6590	0.9510
334.75	0.7630	0.9720
333.15	0.8190	0.9780
331.25	0.8970	0.9880

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE	x1[mol/mol] of Acetone (2) - Liquid
374.5	0.1240
361.64	0.2420
353.15	0.3540
347.36	0.4600
343.18	0.5610
339.49	0.6570
336.47	0.7490
334.05	0.8360
331.83	0.9200

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Acetone (2) - Liquid	y1[mol/mol] of Acetone (2) - Vapour
9.733	0.1600	0.9140
15.465	0.4350	0.9610
19.865	0.6500	0.9750
21.865	0.7900	0.9840
24.265	0.9050	0.9890
25.331	0.9510	0.9910

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test

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