Mixture of Acetic acid, butyl ester + Mesitylene

Datasets

1. n₀ - Refractive index (Na D-line)
2. ρ_l - Mass density, kg/m3
3. γ - Surface tension liquid-gas, N/m

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetic acid, butyl ester (1) - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
0.0516	293.15	1.4941
0.0516	298.15	1.4916
0.0516	303.15	1.4891
0.0516	308.15	1.4865
0.0516	313.15	1.484
0.1002	293.15	1.489
0.1002	298.15	1.4866
0.1002	303.15	1.4841
0.1002	308.15	1.4816
0.1002	313.15	1.4789
0.1506	293.15	1.4839
0.1506	298.15	1.4814
0.1506	303.15	1.4788
0.1506	308.15	1.4763
0.1506	313.15	1.4737
0.2009	293.15	1.4787
0.2009	298.15	1.4762
0.2009	303.15	1.4737
0.2009	308.15	1.4711
0.2009	313.15	1.4686
0.2516	293.15	1.4734
0.2516	298.15	1.4709
0.2516	303.15	1.4684
0.2516	308.15	1.4659
0.2516	313.15	1.4634
0.2995	293.15	1.4684
0.2995	298.15	1.4659
0.2995	303.15	1.4634
0.2995	308.15	1.4609
0.2995	313.15	1.4584
0.3481	293.15	1.4633
0.3481	298.15	1.4608
0.3481	303.15	1.4584
0.3481	308.15	1.4558
0.3481	313.15	1.4533
0.3998	293.15	1.4579
0.3998	298.15	1.4554
0.3998	303.15	1.4529
0.3998	308.15	1.4504
0.3998	313.15	1.4479
0.4499	293.15	1.4527
0.4499	298.15	1.4501
0.4499	303.15	1.4477
0.4499	308.15	1.4451
0.4499	313.15	1.4426
0.5012	293.15	1.4472
0.5012	298.15	1.4447
0.5012	303.15	1.4423
0.5012	308.15	1.4397
0.5012	313.15	1.4373
0.5517	293.15	1.4419
0.5517	298.15	1.4394
0.5517	303.15	1.4369
0.5517	308.15	1.4344
0.5517	313.15	1.4319
0.5990	293.15	1.4369
0.5990	298.15	1.4344
0.5990	303.15	1.4319
0.5990	308.15	1.4294
0.5990	313.15	1.4269
0.6518	293.15	1.4313
0.6518	298.15	1.4288
0.6518	303.15	1.4264
0.6518	308.15	1.4238
0.6518	313.15	1.4213
0.7020	293.15	1.426
0.7020	298.15	1.4235
0.7020	303.15	1.421
0.7020	308.15	1.4185
0.7020	313.15	1.416
0.7495	293.15	1.4209
0.7495	298.15	1.4184
0.7495	303.15	1.416
0.7495	308.15	1.4134
0.7495	313.15	1.411
0.8007	293.15	1.4154
0.8007	298.15	1.413
0.8007	303.15	1.4105
0.8007	308.15	1.408
0.8007	313.15	1.4055
0.8531	293.15	1.4098
0.8531	298.15	1.4074
0.8531	303.15	1.4049
0.8531	308.15	1.4024
0.8531	313.15	1.4
0.8998	293.15	1.4048
0.8998	298.15	1.4024
0.8998	303.15	1.4
0.8998	308.15	1.3975
0.8998	313.15	1.395
0.9494	293.15	1.3995
0.9494	298.15	1.3971
0.9494	303.15	1.3947
0.9494	308.15	1.3922
0.9494	313.15	1.3897

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	861.04
298.15	0.0736	861.9
298.15	0.1009	862.23
298.15	0.1521	862.84
298.15	0.2018	863.45
298.15	0.2523	864.09
298.15	0.3003	864.7
298.15	0.3499	865.36
298.15	0.4005	866.03
298.15	0.4500	866.72
298.15	0.4996	867.44
298.15	0.5446	868.11
298.15	0.5979	868.92
298.15	0.6503	869.76
298.15	0.7016	870.59
298.15	0.7504	871.44
298.15	0.8005	872.32
298.15	0.8460	873.17
298.15	0.8981	874.13
298.15	0.9333	874.87
298.15	1.0000	876.18
303.15	0.0000	856.96
303.15	0.1005	858.04
303.15	0.1997	859.17
303.15	0.3000	860.37
303.15	0.3996	861.61
303.15	0.5007	862.98
303.15	0.6007	864.4
303.15	0.7001	865.94
303.15	0.7971	867.56
303.15	0.9009	869.4
303.15	1.0000	871.31
308.15	0.0000	852.84
308.15	0.1002	853.8
308.15	0.1986	854.82
308.15	0.2997	855.94
308.15	0.4003	857.12
308.15	0.5007	858.39
308.15	0.5997	859.71
308.15	0.7005	861.18
308.15	0.8000	862.75
308.15	0.9006	864.44
308.15	1.0000	866.24
313.15	0.0000	848.74
313.15	0.0498	849.12
313.15	0.0997	849.59
313.15	0.1500	850.08
313.15	0.2012	850.6
313.15	0.2502	851.13
313.15	0.2996	851.64
313.15	0.3507	852.22
313.15	0.3987	852.78
313.15	0.4497	853.39
313.15	0.5008	854.0
313.15	0.5499	854.62
313.15	0.5964	855.24
313.15	0.6503	855.99
313.15	0.6995	856.68
313.15	0.7499	857.4
313.15	0.7994	858.19
313.15	0.8499	858.99
313.15	0.9000	859.83
313.15	0.9495	860.67
313.15	1.0000	861.57

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetic acid, butyl ester (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0281
298.15	0.1009	0.0277
298.15	0.2018	0.0273
298.15	0.3003	0.0270
298.15	0.4005	0.0266
298.15	0.4996	0.0263
298.15	0.5979	0.0259
298.15	0.7016	0.0256
298.15	0.8005	0.0254
298.15	0.8981	0.0251
298.15	1.0000	0.0249
303.15	0.0000	0.0277
303.15	0.1005	0.0273
303.15	0.1997	0.0269
303.15	0.3000	0.0265
303.15	0.3996	0.0261
303.15	0.5007	0.0258
303.15	0.6007	0.0255
303.15	0.7001	0.0251
303.15	0.7971	0.0249
303.15	0.9009	0.0246
303.15	1.0000	0.0244
308.15	0.0000	0.0272
308.15	0.1002	0.0268
308.15	0.1986	0.0264
308.15	0.2997	0.0261
308.15	0.4003	0.0257
308.15	0.5007	0.0253
308.15	0.5997	0.0249
308.15	0.7005	0.0246
308.15	0.8000	0.0243
308.15	0.9006	0.0241
308.15	1.0000	0.0238
313.15	0.0000	0.0268
313.15	0.0997	0.0264
313.15	0.2012	0.0260
313.15	0.2996	0.0256
313.15	0.3987	0.0252
313.15	0.5008	0.0248
313.15	0.5964	0.0244
313.15	0.6995	0.0241
313.15	0.7994	0.0238
313.15	0.9000	0.0235
313.15	1.0000	0.0233

Sources

• Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
• Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K

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