Mixture of Benzene, nitro- + Toluene

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1202.95
293.15	0.0629	1181.81
293.15	0.1476	1153.37
293.15	0.2138	1131.14
293.15	0.2787	1109.35
293.15	0.3587	1082.5
293.15	0.4142	1063.89
293.15	0.4831	1040.77
293.15	0.5232	1027.31
293.15	0.5771	1009.22
293.15	0.6321	990.75
293.15	0.6832	973.59
293.15	0.7234	960.08
293.15	0.8032	933.21
293.15	0.8562	915.34
293.15	0.9213	893.37
293.15	1.0000	866.75
303.15	0.0000	1193.56
303.15	0.0567	1174.37
303.15	0.1332	1148.52
303.15	0.1850	1131.03
303.15	0.2304	1115.73
303.15	0.2798	1099.1
303.15	0.3674	1069.64
303.15	0.4026	1057.82
303.15	0.4656	1036.69
303.15	0.5072	1022.73
303.15	0.5782	998.94
303.15	0.6576	972.35
303.15	0.7235	950.27
303.15	0.7965	925.82
303.15	0.8643	903.09
303.15	0.9354	879.23
303.15	1.0000	857.53
313.15	0.0000	1183.37
313.15	0.0674	1160.46
313.15	0.1534	1131.33
313.15	0.1978	1116.33
313.15	0.2576	1096.15
313.15	0.3254	1073.34
313.15	0.3789	1055.38
313.15	0.4577	1028.98
313.15	0.5067	1012.59
313.15	0.5564	996.0
313.15	0.6134	976.98
313.15	0.6740	956.78
313.15	0.7435	933.64
313.15	0.8134	910.37
313.15	0.8650	893.2
313.15	0.9134	877.09
313.15	1.0000	848.25
323.15	0.0000	1172.38
323.15	0.0479	1156.07
323.15	0.1289	1128.59
323.15	0.1874	1108.81
323.15	0.2671	1081.99
323.15	0.3371	1058.51
323.15	0.3961	1038.77
323.15	0.4628	1016.54
323.15	0.5342	992.79
323.15	0.6056	969.11
323.15	0.6854	942.7
323.15	0.7245	929.78
323.15	0.8056	903.01
323.15	0.8543	886.94
323.15	0.8965	873.03
323.15	0.9423	857.93
323.15	1.0000	838.9
333.15	0.0000	1160.59
333.15	0.0575	1141.04
333.15	0.1435	1111.97
333.15	0.2345	1081.38
333.15	0.2978	1060.21
333.15	0.3534	1041.68
333.15	0.4213	1019.15
333.15	0.4896	996.55
333.15	0.5634	972.23
333.15	0.6233	952.54
333.15	0.6856	932.12
333.15	0.7435	913.17
333.15	0.7947	896.44
333.15	0.8634	874.02
333.15	0.9067	859.9
333.15	0.9424	848.26
333.15	1.0000	829.5
343.15	0.0000	1148.0
343.15	0.0523	1130.3
343.15	0.1389	1101.17
343.15	0.1924	1083.27
343.15	0.2684	1057.97
343.15	0.3289	1037.94
343.15	0.3889	1018.15
343.15	0.4521	997.4
343.15	0.5123	977.7
343.15	0.5931	951.38
343.15	0.6532	931.86
343.15	0.7234	909.14
343.15	0.7923	886.89
343.15	0.8534	867.19
343.15	0.8811	858.27
343.15	0.9421	838.64
343.15	1.0000	820.03
353.15	0.0000	1134.61
353.15	0.0442	1119.76
353.15	0.1247	1092.87
353.15	0.1842	1073.14
353.15	0.2479	1052.11
353.15	0.2943	1036.87
353.15	0.3479	1019.33
353.15	0.4109	998.83
353.15	0.4671	980.61
353.15	0.5239	962.27
353.15	0.5791	944.5
353.15	0.6321	927.5
353.15	0.7913	876.69
353.15	0.8423	860.48
353.15	0.8742	850.36
353.15	0.9311	832.32
353.15	1.0000	810.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1202.95
293.15	0.0629	1181.81
293.15	0.1476	1153.37
293.15	0.2138	1131.14
293.15	0.2787	1109.35
293.15	0.3587	1082.5
293.15	0.4142	1063.89
293.15	0.4831	1040.77
293.15	0.5232	1027.31
293.15	0.5771	1009.22
293.15	0.6321	990.75
293.15	0.6832	973.59
293.15	0.7234	960.08
293.15	0.8032	933.21
293.15	0.8562	915.34
293.15	0.9213	893.37
293.15	1.0000	866.75
303.15	0.0000	1193.56
303.15	0.0567	1174.37
303.15	0.1332	1148.52
303.15	0.1850	1131.03
303.15	0.2304	1115.73
303.15	0.2798	1099.1
303.15	0.3674	1069.64
303.15	0.4026	1057.82
303.15	0.4656	1036.69
303.15	0.5072	1022.73
303.15	0.5782	998.94
303.15	0.6576	972.35
303.15	0.7235	950.27
303.15	0.7965	925.82
303.15	0.8643	903.09
303.15	0.9354	879.23
303.15	1.0000	857.53
313.15	0.0000	1183.37
313.15	0.0674	1160.46
313.15	0.1534	1131.33
313.15	0.1978	1116.33
313.15	0.2576	1096.15
313.15	0.3254	1073.34
313.15	0.3789	1055.38
313.15	0.4577	1028.98
313.15	0.5067	1012.59
313.15	0.5564	996.0
313.15	0.6134	976.98
313.15	0.6740	956.78
313.15	0.7435	933.64
313.15	0.8134	910.37
313.15	0.8650	893.2
313.15	0.9134	877.09
313.15	1.0000	848.25
323.15	0.0000	1172.38
323.15	0.0479	1156.07
323.15	0.1289	1128.59
323.15	0.1874	1108.81
323.15	0.2671	1081.99
323.15	0.3371	1058.51
323.15	0.3961	1038.77
323.15	0.4628	1016.54
323.15	0.5342	992.79
323.15	0.6056	969.11
323.15	0.6854	942.7
323.15	0.7245	929.78
323.15	0.8056	903.01
323.15	0.8543	886.94
323.15	0.8965	873.03
323.15	0.9423	857.93
323.15	1.0000	838.9
333.15	0.0000	1160.59
333.15	0.0575	1141.04
333.15	0.1435	1111.97
333.15	0.2345	1081.38
333.15	0.2978	1060.21
333.15	0.3534	1041.68
333.15	0.4213	1019.15
333.15	0.4896	996.55
333.15	0.5634	972.23
333.15	0.6233	952.54
333.15	0.6856	932.12
333.15	0.7435	913.17
333.15	0.7947	896.44
333.15	0.8634	874.02
333.15	0.9067	859.9
333.15	0.9424	848.26
333.15	1.0000	829.5
343.15	0.0000	1148.0
343.15	0.0523	1130.3
343.15	0.1389	1101.17
343.15	0.1924	1083.27
343.15	0.2684	1057.97
343.15	0.3289	1037.94
343.15	0.3889	1018.15
343.15	0.4521	997.4
343.15	0.5123	977.7
343.15	0.5931	951.38
343.15	0.6532	931.86
343.15	0.7234	909.14
343.15	0.7923	886.89
343.15	0.8534	867.19
343.15	0.8811	858.27
343.15	0.9421	838.64
343.15	1.0000	820.03
353.15	0.0000	1134.61
353.15	0.0442	1119.76
353.15	0.1247	1092.87
353.15	0.1842	1073.14
353.15	0.2479	1052.11
353.15	0.2943	1036.87
353.15	0.3479	1019.33
353.15	0.4109	998.83
353.15	0.4671	980.61
353.15	0.5239	962.27
353.15	0.5791	944.5
353.15	0.6321	927.5
353.15	0.7913	876.69
353.15	0.8423	860.48
353.15	0.8742	850.36
353.15	0.9311	832.32
353.15	1.0000	810.5

Sources

• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K