Mixture of Acetone + Water

Datasets

1. Activity coefficient (2)
2. Henry's Law constant (mole fraction scale), kPa (5)
3. n₀ - Refractive index (Na D-line)
4. ρ_l - Mass density, kg/m3 (3)
5. γ - Surface tension liquid-gas, N/m
6. Binary diffusion coefficient, m2/s (3)
7. Vapor Liquid Equilibrium at Constant Pressure (3)

Activity coefficient of Acetone (1) [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Acetone (1) - Liquid
298.01	7.62
298.01	7.68
298.03	7.64
298.03	7.7
298.04	7.68
298.04	7.74
298.17	7.7

Activity coefficient of Acetone (1) [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Acetone (1) - Liquid
303.25	8.02
313.25	9.2
323.25	9.81
333.25	10.3

Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid
323.15	699.1
333.15	1033.5
343.15	1519.9
353.15	2148.1

Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid
298.01	233.0
298.01	235.0
298.03	234.0
298.03	236.0
298.04	236.0
298.04	237.0
298.17	237.0

Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) - Liquid
274.15	0.2310
294.65	1.442
294.65	1.263
296.15	1.133
310.15	7.555
320.15	11.46
331.15	16.01
333.15	41.15

Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid
278.20	56.0
283.20	75.0
288.20	100.0
293.20	130.0
298.20	170.0

Henry's Law constant (amount concentration scale), kPa*dm3/mol of Acetone (1) [ref]

Operational condition: Amount concentration (molarity), mol/dm3 = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (amount concentration scale), kPa*dm3/mol of Acetone (1) - Liquid
276.00	14591.0
279.00	11044.0
283.00	8511.0
288.00	6991.0
293.00	3749.0

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Acetone (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0502	1.3422
0.0993	1.3499
0.1502	1.3549
0.1996	1.3583
0.2496	1.3604
0.3007	1.3616
0.3507	1.3621
0.4003	1.3623
0.4509	1.3621
0.4992	1.3618
0.5489	1.3614
0.5990	1.3609
0.6506	1.3603
0.6996	1.3602
0.7014	1.3597
0.7467	1.3591
0.8011	1.3592
0.8015	1.3583
0.8460	1.3577
0.8969	1.3569
0.9005	1.3572
0.9451	1.3564

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Acetone (1) - Liquid	Mass density, kg/m3 - Liquid
0.0502	977.0
0.0993	959.3
0.1502	942.2
0.1996	926.6
0.2496	911.8
0.3007	897.6
0.3507	884.8
0.4003	873.1
0.4509	862.1
0.4992	852.5
0.5489	843.5
0.5990	835.0
0.6506	827.0
0.6996	819.9
0.7014	819.6
0.7467	813.4
0.8011	806.2
0.8015	806.3
0.8460	800.8
0.8969	794.9
0.9005	794.5
0.9451	789.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Mole fraction of Acetone (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	283.15	999.691
0.0000	288.15	999.083
0.0000	293.14	998.181
0.0000	298.15	997.019
0.0000	303.14	995.617
0.0000	308.15	994.001
0.0000	313.15	992.181
0.0000	318.14	990.13
0.0000	323.14	988.003
0.0988	283.15	966.507
0.0988	288.15	963.567
0.0988	293.15	960.497
0.0988	298.14	957.313
0.0988	303.15	954.01
0.0988	308.15	950.61
0.0988	313.14	947.117
0.0988	318.15	943.497
0.0988	323.15	939.767
0.2193	283.15	932.823
0.2193	288.15	928.61
0.2193	293.14	924.322
0.2193	298.14	919.968
0.2193	303.14	915.544
0.2193	308.15	911.052
0.2193	313.14	906.488
0.2193	318.14	901.855
0.2193	323.15	897.151
0.2973	283.15	913.382
0.2973	288.15	908.777
0.2973	293.14	904.105
0.2973	298.14	899.375
0.2973	303.14	894.587
0.2973	308.15	889.735
0.2973	313.14	884.822
0.2973	318.14	879.849
0.2973	323.14	874.812
0.3998	283.15	889.08
0.3998	288.15	884.145
0.3998	293.14	879.148
0.3998	298.14	874.098
0.3998	303.14	868.996
0.3998	308.15	863.836
0.3998	313.14	858.617
0.3998	318.14	853.341
0.3998	323.14	848.021
0.4986	283.15	868.988
0.4986	288.15	863.861
0.4986	293.15	858.674
0.4986	298.15	853.436
0.4986	303.14	848.142
0.4986	308.15	842.791
0.4986	313.15	837.381
0.4986	318.14	831.924
0.4986	323.14	826.399
0.5903	283.15	853.092
0.5903	288.15	847.829
0.5903	293.15	842.508
0.5903	298.14	837.135
0.5903	303.14	831.707
0.5903	308.14	826.22
0.5903	313.14	820.677
0.5903	318.15	815.068
0.5903	323.15	809.395
0.6984	283.15	836.647
0.6984	288.15	831.252
0.6984	293.15	825.797
0.6984	298.14	820.292
0.6984	303.14	814.735
0.6984	308.15	809.12
0.6984	313.14	803.446
0.6984	318.15	797.707
0.6984	323.14	791.9
0.7934	283.15	824.028
0.7934	288.15	818.534
0.7934	293.15	812.982
0.7934	298.14	807.383
0.7934	303.14	801.735
0.7934	308.15	796.028
0.7934	313.14	790.262
0.7934	318.14	784.437
0.7934	323.14	778.546
0.8916	283.15	812.997
0.8916	288.15	807.424
0.8916	293.15	801.797
0.8916	298.14	796.13
0.8916	303.14	790.413
0.8916	308.15	784.645
0.8916	313.14	778.818
0.8916	318.14	772.936
0.8916	323.14	766.99
1.0000	283.15	801.669
1.0000	288.15	796.037
1.0000	293.15	790.355
1.0000	298.15	784.638
1.0000	303.14	778.876
1.0000	308.15	773.065
1.0000	313.14	767.205
1.0000	318.14	761.288
1.0000	323.14	755.314

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetone (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	999.12
288.15	0.0099	994.9
288.15	0.0500	981.27
288.15	0.1000	965.81
288.15	0.1500	950.41
288.15	0.2000	935.61
288.15	0.3000	907.7
288.15	0.4000	884.77
288.15	0.5000	863.71
288.15	0.6000	845.83
288.15	0.7000	830.7
288.15	0.8000	818.04
288.15	0.9000	805.86
288.15	1.0000	795.65
293.15	0.0000	998.22
293.15	0.0099	993.87
293.15	0.0500	979.34
293.15	0.1000	962.9
293.15	0.1500	946.79
293.15	0.2000	931.54
293.15	0.3000	903.09
293.15	0.4000	879.81
293.15	0.5000	858.56
293.15	0.6000	840.53
293.15	0.7000	825.3
293.15	0.8000	812.56
293.15	0.9000	800.27
293.15	1.0000	790.04
298.15	0.0000	997.06
298.15	0.0099	992.55
298.15	0.0500	977.21
298.15	0.1000	959.83
298.15	0.1500	943.05
298.15	0.2000	927.37
298.15	0.3000	898.35
298.15	0.4000	874.8
298.15	0.5000	853.35
298.15	0.6000	835.15
298.15	0.7000	819.8
298.15	0.8000	806.97
298.15	0.9000	794.6
298.15	1.0000	784.33
303.15	0.0000	995.67
303.15	0.0099	991.0
303.15	0.0500	974.89
303.15	0.1000	956.64
303.15	0.1500	939.23
303.15	0.2000	923.1
303.15	0.3000	893.54
303.15	0.4000	869.68
303.15	0.5000	848.07
303.15	0.6000	829.71
303.15	0.7000	814.25
303.15	0.8000	801.32
303.15	0.9000	788.88
303.15	1.0000	778.57
308.15	0.0000	994.04
308.15	0.0099	989.16
308.15	0.0500	972.41
308.15	0.1000	953.33
308.15	0.1500	935.32
308.15	0.2000	918.78
308.15	0.3000	888.68
308.15	0.4000	864.53
308.15	0.5000	842.72
308.15	0.6000	824.22
308.15	0.7000	808.63
308.15	0.8000	795.62
308.15	0.9000	783.11
308.15	1.0000	772.76
313.15	0.0000	992.23
313.15	0.0099	987.26
313.15	0.0500	969.77
313.15	0.1000	949.91
313.15	0.1500	931.31
313.15	0.2000	914.37
313.15	0.3000	883.75
313.15	0.4000	859.33
313.15	0.5000	837.31
313.15	0.6000	818.66
313.15	0.7000	802.96
313.15	0.8000	789.84
313.15	0.9000	777.29
313.15	1.0000	766.91
318.15	0.0000	990.23
318.15	0.0099	985.07
318.15	0.0500	966.73
318.15	0.1000	946.37
318.15	0.1500	927.21
318.15	0.2000	909.89
318.15	0.3000	878.76
318.15	0.4000	854.06
318.15	0.5000	831.85
318.15	0.6000	813.05
318.15	0.7000	797.22
318.15	0.8000	784.05
318.15	0.9000	771.4
318.15	1.0000	760.99
323.15	0.0000	988.01
323.15	0.0099	982.76
323.15	0.0500	963.1
323.15	0.1000	942.68
323.15	0.1500	923.0
323.15	0.2000	905.19
323.15	0.3000	873.7
323.15	0.4000	848.74
323.15	0.5000	826.32
323.15	0.6000	807.35
323.15	0.7000	791.42
323.15	0.8000	778.16
323.15	0.9000	765.46
323.15	1.0000	755.02
328.15	0.0000	985.69
328.15	0.0099	980.29
328.15	0.0500	959.94
328.15	0.1000	938.87
328.15	0.1500	918.72
328.15	0.2000	900.64
328.15	0.3000	868.56
328.15	0.4000	843.31
328.15	0.5000	820.73
328.15	0.6000	801.6
328.15	0.7000	785.55
328.15	0.8000	772.2
328.15	0.9000	759.81
328.15	1.0000	748.98

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetone (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
288.15	0.0000	0.0735
288.15	0.0099	0.0626
288.15	0.0500	0.0478
288.15	0.0999	0.0403
288.15	0.1500	0.0357
288.15	0.1999	0.0337
288.15	0.2999	0.0306
288.15	0.4000	0.0292
288.15	0.4999	0.0282
288.15	0.5999	0.0273
288.15	0.6999	0.0267
288.15	0.7999	0.0258
288.15	0.8999	0.0251
288.15	1.0000	0.0243
298.15	0.0000	0.0720
298.15	0.0099	0.0610
298.15	0.0500	0.0461
298.15	0.0999	0.0391
298.15	0.1500	0.0344
298.15	0.1999	0.0322
298.15	0.2999	0.0294
298.15	0.4000	0.0280
298.15	0.4999	0.0270
298.15	0.5999	0.0260
298.15	0.6999	0.0254
298.15	0.7999	0.0245
298.15	0.8999	0.0238
298.15	1.0000	0.0230
308.15	0.0000	0.0704
308.15	0.0099	0.0593
308.15	0.0500	0.0448
308.15	0.0999	0.0379
308.15	0.1500	0.0331
308.15	0.1999	0.0307
308.15	0.2999	0.0281
308.15	0.4000	0.0268
308.15	0.4999	0.0258
308.15	0.5999	0.0248
308.15	0.6999	0.0243
308.15	0.7999	0.0232
308.15	0.8999	0.0226
308.15	1.0000	0.0217
318.15	0.0000	0.0688
318.15	0.0099	0.0581
318.15	0.0500	0.0437
318.15	0.0999	0.0369
318.15	0.1500	0.0320
318.15	0.1999	0.0294
318.15	0.2999	0.0270
318.15	0.4000	0.0255
318.15	0.4999	0.0245
318.15	0.5999	0.0236
318.15	0.6999	0.0229
318.15	0.7999	0.0220
318.15	0.8999	0.0212
318.15	1.0000	0.0204
328.15	0.0000	0.0671
328.15	0.0099	0.0577
328.15	0.0500	0.0429
328.15	0.0999	0.0357
328.15	0.1500	0.0308
328.15	0.1999	0.0283
328.15	0.2999	0.0257
328.15	0.4000	0.0242
328.15	0.4999	0.0233
328.15	0.5999	0.0223
328.15	0.6999	0.0217
328.15	0.7999	0.0209
328.15	0.8999	0.0202
328.15	1.0000	0.0192

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Mole fraction of Acetone (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0040	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9750	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Mole fraction of Acetone (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0040	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9750	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetone (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0018	0.0000
0.0018	0.0000
0.0041	0.0000
0.0043	0.0000
0.0045	0.0000
0.0979	0.0000
0.1061	0.0000
0.2916	0.0000
0.3068	0.0000
0.4818	0.0000
0.5161	0.0000
0.5234	0.0000
0.5375	0.0000
0.6695	0.0000
0.6698	0.0000
0.7099	0.0000
0.8547	0.0000
0.9774	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetone (1) - Liquid	y1[mol/mol] of Acetone (1) - Vapour
368.25	0.0080	0.1380
363.25	0.0160	0.2770
355.25	0.0330	0.4790
349.35	0.0520	0.6040
345.35	0.0720	0.6750
342.65	0.0940	0.7190
340.75	0.1170	0.7380
338.15	0.1710	0.7760
336.45	0.2370	0.8000
335.15	0.3180	0.8220
334.15	0.4200	0.8390
333.05	0.5540	0.8630
331.35	0.7360	0.9090

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 344.73 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetone (1) - Liquid	y1[mol/mol] of Acetone (1) - Vapour
395.65	0.0170	0.3490
393.15	0.0240	0.3980
385.15	0.0550	0.5180
379.15	0.1070	0.6080
375.95	0.1940	0.6700
374.45	0.2730	0.6950
373.05	0.3880	0.7180
372.15	0.5450	0.7470
371.95	0.6330	0.7680
371.75	0.7780	0.8300
371.55	0.8900	0.9030
371.35	0.9500	0.9510

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 689.48 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetone (1) - Liquid	y1[mol/mol] of Acetone (1) - Vapour
423.85	0.0140	0.2490
415.45	0.0360	0.3950
409.55	0.0780	0.5070
404.25	0.1440	0.5820
402.75	0.2290	0.6180
402.15	0.3410	0.6500
401.45	0.4440	0.6650
399.75	0.5590	0.7000
398.85	0.7540	0.7810
398.55	0.8420	0.8450
399.15	0.9250	0.9120

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• A relative headspace method for Henry s constants of volatile organic compounds
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
• Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
• Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Surface Tension of the Ternary System Water + Acetone + Toluene
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K

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