Mixture of N,N-Dimethylacetamide + Ethyl Acetate

Datasets

1. η - Viscosity, Pa*s (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0004
0.0392	0.0004
0.0791	0.0005
0.1560	0.0005
0.2331	0.0005
0.3109	0.0006
0.3875	0.0006
0.4646	0.0006
0.5410	0.0007
0.6137	0.0007
0.6931	0.0008
0.7718	0.0008
0.8145	0.0008
0.8896	0.0009
0.9558	0.0009
1.0000	0.0009

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0004
0.0392	0.0004
0.0791	0.0005
0.1560	0.0005
0.2331	0.0005
0.3109	0.0006
0.3875	0.0006
0.4646	0.0006
0.5410	0.0007
0.6137	0.0007
0.6931	0.0008
0.7718	0.0008
0.8145	0.0008
0.8896	0.0009
0.9558	0.0009
1.0000	0.0009

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 1307 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0476	0.0280
0.0954	0.0527
0.1435	0.0786
0.1918	0.1000
0.2404	0.1190
0.2892	0.1370
0.3383	0.1510
0.3876	0.1640
0.4372	0.1730
0.4870	0.1800
0.5371	0.1840
0.5875	0.1830
0.6381	0.1800
0.6890	0.1710
0.7401	0.1600
0.7916	0.1440
0.8433	0.1200
0.8952	0.0888
0.9475	0.0499

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 1307 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0476	0.0280
0.0954	0.0527
0.1435	0.0786
0.1918	0.1000
0.2404	0.1190
0.2892	0.1370
0.3383	0.1510
0.3876	0.1640
0.4372	0.1730
0.4870	0.1800
0.5371	0.1840
0.5875	0.1830
0.6381	0.1800
0.6890	0.1710
0.7401	0.1600
0.7916	0.1440
0.8433	0.1200
0.8952	0.0888
0.9475	0.0499

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	5.31
0.0025	5.67
0.0048	6.02
0.0073	6.39
0.0096	6.73
0.0127	7.19
0.0157	7.65
0.0220	8.57
0.0285	9.52
0.0398	11.11
0.0553	13.31
0.0743	15.92
0.0976	19.07
0.1264	22.86
0.1577	26.86
0.1908	30.97
0.2259	35.18
0.2630	39.50
0.2996	43.64
0.3367	47.70
0.3701	51.27
0.4023	54.64
0.4343	57.90
0.4428	58.82
0.4656	61.03
0.4706	61.59
0.4946	63.89
0.4980	64.27
0.5206	66.40
0.5288	67.16
0.5470	68.94
0.5615	70.27
0.5950	73.42
0.6288	76.56
0.6637	79.78
0.7027	83.34
0.7411	86.86
0.7799	90.40
0.8161	93.74
0.8510	96.99
0.8838	100.11
0.9135	102.99
0.9369	105.33
0.9555	107.20
0.9700	108.70
0.9794	109.66
0.9859	110.30
0.9902	110.76
0.9934	111.08
0.9960	111.35
0.9977	111.52
0.9988	111.62
0.9994	111.69
1.0000	111.76

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	5.31
0.0025	5.67
0.0048	6.02
0.0073	6.39
0.0096	6.73
0.0127	7.19
0.0157	7.65
0.0220	8.57
0.0285	9.52
0.0398	11.11
0.0553	13.31
0.0743	15.92
0.0976	19.07
0.1264	22.86
0.1577	26.86
0.1908	30.97
0.2259	35.18
0.2630	39.50
0.2996	43.64
0.3367	47.70
0.3701	51.27
0.4023	54.64
0.4343	57.90
0.4428	58.82
0.4656	61.03
0.4706	61.59
0.4946	63.89
0.4980	64.27
0.5206	66.40
0.5288	67.16
0.5470	68.94
0.5615	70.27
0.5950	73.42
0.6288	76.56
0.6637	79.78
0.7027	83.34
0.7411	86.86
0.7799	90.40
0.8161	93.74
0.8510	96.99
0.8838	100.11
0.9135	102.99
0.9369	105.33
0.9555	107.20
0.9700	108.70
0.9794	109.66
0.9859	110.30
0.9902	110.76
0.9934	111.08
0.9960	111.35
0.9977	111.52
0.9988	111.62
0.9994	111.69
1.0000	111.76

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3699
0.0392	1.3731
0.0791	1.3763
0.1560	1.3824
0.2331	1.3883
0.3109	1.3942
0.3875	1.3999
0.4646	1.4054
0.5410	1.4106
0.6137	1.4153
0.6931	1.4201
0.7718	1.4246
0.8145	1.4269
0.8896	1.4307
0.9558	1.4338
1.0000	1.4357

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3699
0.0392	1.3731
0.0791	1.3763
0.1560	1.3824
0.2331	1.3883
0.3109	1.3942
0.3875	1.3999
0.4646	1.4054
0.5410	1.4106
0.6137	1.4153
0.6931	1.4201
0.7718	1.4246
0.8145	1.4269
0.8896	1.4307
0.9558	1.4338
1.0000	1.4357

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	894.6
0.0392	896.84
0.0791	898.95
0.1560	902.75
0.2331	906.43
0.3109	909.97
0.3875	913.34
0.4646	916.63
0.5410	919.8
0.6137	922.68
0.6931	925.71
0.7718	928.62
0.8145	930.15
0.8896	932.81
0.9558	935.14
1.0000	936.7

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of N,N-Dimethylacetamide (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	894.6
0.0392	896.84
0.0791	898.95
0.1560	902.75
0.2331	906.43
0.3109	909.97
0.3875	913.34
0.4646	916.63
0.5410	919.8
0.6137	922.68
0.6931	925.71
0.7718	928.62
0.8145	930.15
0.8896	932.81
0.9558	935.14
1.0000	936.7

Sources

• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of N,N-Dimethylacetamide (1) + 2-Methylbutan-2-ol (2) + Ethyl Acetate (3) at 298.15 K for the Liquid Region and at Ambient Pressure