Mixture of Toluene + 2-Propenoic acid, butyl ester

Datasets

1. ρ_l - Mass density, kg/m3 (4)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propenoic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	871.79
288.15	0.0704	875.4
288.15	0.1402	878.72
288.15	0.2054	881.63
288.15	0.2799	884.72
288.15	0.3604	887.81
288.15	0.4338	890.4
288.15	0.5098	892.88
288.15	0.5836	895.08
288.15	0.6584	897.1
288.15	0.7198	898.6
288.15	0.7912	900.18
288.15	0.8578	901.48
288.15	0.9324	902.74
288.15	1.0000	903.6
293.15	0.0000	867.08
293.15	0.0704	870.63
293.15	0.1402	873.92
293.15	0.2054	876.8
293.15	0.2799	879.86
293.15	0.3604	882.94
293.15	0.4338	885.52
293.15	0.5098	888.0
293.15	0.5836	890.19
293.15	0.6584	892.22
293.15	0.7198	893.73
293.15	0.7912	895.32
293.15	0.8578	896.64
293.15	0.9324	897.93
293.15	1.0000	898.85
298.15	0.0000	862.36
298.15	0.0704	865.86
298.15	0.1402	869.12
298.15	0.2054	871.97
298.15	0.2799	875.0
298.15	0.3604	878.07
298.15	0.4338	880.64
298.15	0.5098	883.12
298.15	0.5836	885.31
298.15	0.6584	887.34
298.15	0.7198	888.86
298.15	0.7912	890.46
298.15	0.8578	891.8
298.15	0.9324	893.12
298.15	1.0000	894.1
303.15	0.0000	857.64
303.15	0.0704	861.09
303.15	0.1402	864.32
303.15	0.2054	867.14
303.15	0.2799	870.15
303.15	0.3604	873.2
303.15	0.4338	875.77
303.15	0.5098	878.24
303.15	0.5836	880.43
303.15	0.6584	882.46
303.15	0.7198	883.99
303.15	0.7912	885.6
303.15	0.8578	886.96
303.15	0.9324	888.31
303.15	1.0000	889.35
308.15	0.0000	852.93
308.15	0.0704	856.32
308.15	0.1402	859.52
308.15	0.2054	862.31
308.15	0.2799	865.31
308.15	0.3604	868.34
308.15	0.4338	870.9
308.15	0.5098	873.36
308.15	0.5836	875.55
308.15	0.6584	877.58
308.15	0.7198	879.12
308.15	0.7912	880.75
308.15	0.8578	882.12
308.15	0.9324	883.5
308.15	1.0000	884.6
313.15	0.0000	848.21
313.15	0.0704	851.55
313.15	0.1402	854.72
313.15	0.2054	857.48
313.15	0.2799	860.47
313.15	0.3604	863.48
313.15	0.4338	866.03
313.15	0.5098	868.48
313.15	0.5836	870.67
313.15	0.6584	872.7
313.15	0.7198	874.25
313.15	0.7912	875.9
313.15	0.8578	877.28
313.15	0.9324	878.69
313.15	1.0000	879.85
318.15	0.0000	843.49
318.15	0.0704	846.79
318.15	0.1402	849.92
318.15	0.2054	852.65
318.15	0.2799	855.63
318.15	0.3604	858.62
318.15	0.4338	861.16
318.15	0.5098	863.6
318.15	0.5836	865.79
318.15	0.6584	867.82
318.15	0.7198	869.38
318.15	0.7912	871.05
318.15	0.8578	872.44
318.15	0.9324	873.88
318.15	1.0000	875.1

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	893.955
0.0255	893.406
0.0508	892.895
0.0999	891.775
0.1509	890.523
0.2006	889.277
0.2506	887.998
0.2996	886.7
0.3597	885.033
0.4006	883.858
0.4504	882.402
0.5015	880.847
0.5500	879.307
0.6006	877.659
0.6502	875.977
0.7003	874.219
0.7501	872.408
0.8000	870.53
0.8499	868.551
0.9001	866.487
0.9500	864.338
0.9751	863.216
1.0000	862.11

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propenoic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	871.79
288.15	0.0704	875.4
288.15	0.1402	878.72
288.15	0.2054	881.63
288.15	0.2799	884.72
288.15	0.3604	887.81
288.15	0.4338	890.4
288.15	0.5098	892.88
288.15	0.5836	895.08
288.15	0.6584	897.1
288.15	0.7198	898.6
288.15	0.7912	900.18
288.15	0.8578	901.48
288.15	0.9324	902.74
288.15	1.0000	903.6
293.15	0.0000	867.08
293.15	0.0704	870.63
293.15	0.1402	873.92
293.15	0.2054	876.8
293.15	0.2799	879.86
293.15	0.3604	882.94
293.15	0.4338	885.52
293.15	0.5098	888.0
293.15	0.5836	890.19
293.15	0.6584	892.22
293.15	0.7198	893.73
293.15	0.7912	895.32
293.15	0.8578	896.64
293.15	0.9324	897.93
293.15	1.0000	898.85
298.15	0.0000	862.36
298.15	0.0704	865.86
298.15	0.1402	869.12
298.15	0.2054	871.97
298.15	0.2799	875.0
298.15	0.3604	878.07
298.15	0.4338	880.64
298.15	0.5098	883.12
298.15	0.5836	885.31
298.15	0.6584	887.34
298.15	0.7198	888.86
298.15	0.7912	890.46
298.15	0.8578	891.8
298.15	0.9324	893.12
298.15	1.0000	894.1
303.15	0.0000	857.64
303.15	0.0704	861.09
303.15	0.1402	864.32
303.15	0.2054	867.14
303.15	0.2799	870.15
303.15	0.3604	873.2
303.15	0.4338	875.77
303.15	0.5098	878.24
303.15	0.5836	880.43
303.15	0.6584	882.46
303.15	0.7198	883.99
303.15	0.7912	885.6
303.15	0.8578	886.96
303.15	0.9324	888.31
303.15	1.0000	889.35
308.15	0.0000	852.93
308.15	0.0704	856.32
308.15	0.1402	859.52
308.15	0.2054	862.31
308.15	0.2799	865.31
308.15	0.3604	868.34
308.15	0.4338	870.9
308.15	0.5098	873.36
308.15	0.5836	875.55
308.15	0.6584	877.58
308.15	0.7198	879.12
308.15	0.7912	880.75
308.15	0.8578	882.12
308.15	0.9324	883.5
308.15	1.0000	884.6
313.15	0.0000	848.21
313.15	0.0704	851.55
313.15	0.1402	854.72
313.15	0.2054	857.48
313.15	0.2799	860.47
313.15	0.3604	863.48
313.15	0.4338	866.03
313.15	0.5098	868.48
313.15	0.5836	870.67
313.15	0.6584	872.7
313.15	0.7198	874.25
313.15	0.7912	875.9
313.15	0.8578	877.28
313.15	0.9324	878.69
313.15	1.0000	879.85
318.15	0.0000	843.49
318.15	0.0704	846.79
318.15	0.1402	849.92
318.15	0.2054	852.65
318.15	0.2799	855.63
318.15	0.3604	858.62
318.15	0.4338	861.16
318.15	0.5098	863.6
318.15	0.5836	865.79
318.15	0.6584	867.82
318.15	0.7198	869.38
318.15	0.7912	871.05
318.15	0.8578	872.44
318.15	0.9324	873.88
318.15	1.0000	875.1

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	893.955
0.0255	893.406
0.0508	892.895
0.0999	891.775
0.1509	890.523
0.2006	889.277
0.2506	887.998
0.2996	886.7
0.3597	885.033
0.4006	883.858
0.4504	882.402
0.5015	880.847
0.5500	879.307
0.6006	877.659
0.6502	875.977
0.7003	874.219
0.7501	872.408
0.8000	870.53
0.8499	868.551
0.9001	866.487
0.9500	864.338
0.9751	863.216
1.0000	862.11

Sources

• Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
• Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K