Mixture of Formamide, N,N-dimethyl- + o-Xylene

Datasets

1. ρ_l - Mass density, kg/m3 (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0555	943.56
293.15	0.1111	938.71
293.15	0.1754	933.3
293.15	0.2352	928.47
293.15	0.2952	923.8
293.15	0.3562	919.23
293.15	0.4251	914.29
293.15	0.4865	910.06
293.15	0.5484	905.95
293.15	0.6120	901.89
293.15	0.6785	897.8
293.15	0.7325	894.58
293.15	0.7954	890.96
293.15	0.8654	887.04
293.15	0.9325	883.4
303.15	0.0652	933.58
303.15	0.1251	928.39
303.15	0.1854	923.37
303.15	0.2462	918.5
303.15	0.3125	913.42
303.15	0.3785	908.59
303.15	0.4358	904.56
303.15	0.4962	900.47
303.15	0.5521	896.83
303.15	0.6125	893.04
303.15	0.6784	889.05
303.15	0.7451	885.17
303.15	0.8012	882.01
303.15	0.8658	878.48
303.15	0.9485	874.12
313.15	0.0441	926.11
313.15	0.1025	920.99
313.15	0.1762	914.82
313.15	0.2341	910.18
313.15	0.2951	905.51
313.15	0.3756	899.63
313.15	0.4415	895.06
313.15	0.5012	891.08
313.15	0.5685	886.8
313.15	0.6215	883.55
313.15	0.6865	879.72
313.15	0.7451	876.39
313.15	0.8021	873.25
313.15	0.8654	869.88
313.15	0.9448	865.79
323.15	0.0485	916.16
323.15	0.1124	910.62
323.15	0.1852	904.61
323.15	0.2521	899.35
323.15	0.3251	893.91
323.15	0.3952	888.96
323.15	0.4658	884.2
323.15	0.5315	879.99
323.15	0.5952	876.08
323.15	0.6584	872.37
323.15	0.7251	868.61
323.15	0.7952	864.81
323.15	0.8456	862.18
323.15	0.9012	859.35
323.15	0.9599	856.45
333.15	0.0521	906.08
333.15	0.1245	899.89
333.15	0.1895	894.6
333.15	0.2451	890.29
333.15	0.3021	886.06
333.15	0.3685	881.35
333.15	0.4214	877.76
333.15	0.4912	873.24
333.15	0.5584	869.09
333.15	0.6121	865.92
333.15	0.6725	862.48
333.15	0.7315	859.26
333.15	0.7943	855.95
333.15	0.8651	852.38
333.15	0.9432	848.58
343.15	0.0625	895.2
343.15	0.1325	889.33
343.15	0.1952	884.33
343.15	0.2658	878.99
343.15	0.3321	874.24
343.15	0.3965	869.86
343.15	0.4652	865.41
343.15	0.5325	861.27
343.15	0.5912	857.83
343.15	0.6524	854.4
343.15	0.7125	851.16
343.15	0.7895	847.19
343.15	0.8462	844.4
343.15	0.9012	841.76
343.15	0.9577	839.14
353.15	0.0715	884.27
353.15	0.1252	879.83
353.15	0.1858	875.05
353.15	0.2521	870.08
353.15	0.3215	865.16
353.15	0.3865	860.79
353.15	0.4251	858.31
353.15	0.4851	854.59
353.15	0.5584	850.27
353.15	0.6221	846.71
353.15	0.6825	843.48
353.15	0.7551	839.78
353.15	0.8154	836.84
353.15	0.8851	833.58
353.15	0.9411	831.05

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0555	943.56
293.15	0.1111	938.71
293.15	0.1754	933.3
293.15	0.2352	928.47
293.15	0.2952	923.8
293.15	0.3562	919.23
293.15	0.4251	914.29
293.15	0.4865	910.06
293.15	0.5484	905.95
293.15	0.6120	901.89
293.15	0.6785	897.8
293.15	0.7325	894.58
293.15	0.7954	890.96
293.15	0.8654	887.04
293.15	0.9325	883.4
303.15	0.0652	933.58
303.15	0.1251	928.39
303.15	0.1854	923.37
303.15	0.2462	918.5
303.15	0.3125	913.42
303.15	0.3785	908.59
303.15	0.4358	904.56
303.15	0.4962	900.47
303.15	0.5521	896.83
303.15	0.6125	893.04
303.15	0.6784	889.05
303.15	0.7451	885.17
303.15	0.8012	882.01
303.15	0.8658	878.48
303.15	0.9485	874.12
313.15	0.0441	926.11
313.15	0.1025	920.99
313.15	0.1762	914.82
313.15	0.2341	910.18
313.15	0.2951	905.51
313.15	0.3756	899.63
313.15	0.4415	895.06
313.15	0.5012	891.08
313.15	0.5685	886.8
313.15	0.6215	883.55
313.15	0.6865	879.72
313.15	0.7451	876.39
313.15	0.8021	873.25
313.15	0.8654	869.88
313.15	0.9448	865.79
323.15	0.0485	916.16
323.15	0.1124	910.62
323.15	0.1852	904.61
323.15	0.2521	899.35
323.15	0.3251	893.91
323.15	0.3952	888.96
323.15	0.4658	884.2
323.15	0.5315	879.99
323.15	0.5952	876.08
323.15	0.6584	872.37
323.15	0.7251	868.61
323.15	0.7952	864.81
323.15	0.8456	862.18
323.15	0.9012	859.35
323.15	0.9599	856.45
333.15	0.0521	906.08
333.15	0.1245	899.89
333.15	0.1895	894.6
333.15	0.2451	890.29
333.15	0.3021	886.06
333.15	0.3685	881.35
333.15	0.4214	877.76
333.15	0.4912	873.24
333.15	0.5584	869.09
333.15	0.6121	865.92
333.15	0.6725	862.48
333.15	0.7315	859.26
333.15	0.7943	855.95
333.15	0.8651	852.38
333.15	0.9432	848.58
343.15	0.0625	895.2
343.15	0.1325	889.33
343.15	0.1952	884.33
343.15	0.2658	878.99
343.15	0.3321	874.24
343.15	0.3965	869.86
343.15	0.4652	865.41
343.15	0.5325	861.27
343.15	0.5912	857.83
343.15	0.6524	854.4
343.15	0.7125	851.16
343.15	0.7895	847.19
343.15	0.8462	844.4
343.15	0.9012	841.76
343.15	0.9577	839.14
353.15	0.0715	884.27
353.15	0.1252	879.83
353.15	0.1858	875.05
353.15	0.2521	870.08
353.15	0.3215	865.16
353.15	0.3865	860.79
353.15	0.4251	858.31
353.15	0.4851	854.59
353.15	0.5584	850.27
353.15	0.6221	846.71
353.15	0.6825	843.48
353.15	0.7551	839.78
353.15	0.8154	836.84
353.15	0.8851	833.58
353.15	0.9411	831.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.1 (Liquid)

Mole fraction of o-Xylene (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	420.95
0.0662	417.45
0.1243	415.75
0.1755	414.65
0.2211	414.05
0.2620	413.55
0.2988	413.25
0.3320	412.95
0.3622	412.75
0.3898	412.65
0.4152	412.55
0.4385	412.55
0.4600	412.45
0.4799	412.35
0.4985	412.35
0.5248	412.25
0.5897	412.25
0.6572	412.35
0.7490	412.75
0.8519	413.55
1.0000	415.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.1 (Liquid)

Mole fraction of o-Xylene (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	420.95
0.0662	417.45
0.1243	415.75
0.1755	414.65
0.2211	414.05
0.2620	413.55
0.2988	413.25
0.3320	412.95
0.3622	412.75
0.3898	412.65
0.4152	412.55
0.4385	412.55
0.4600	412.45
0.4799	412.35
0.4985	412.35
0.5248	412.25
0.5897	412.25
0.6572	412.35
0.7490	412.75
0.8519	413.55
1.0000	415.35

Sources

• Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
• Densities and volumetric properties of binary mixtures of xylene with N,N-dimethylformamide at different temperatures