Mixture of Benzene, nitro- + Styrene

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 Styrene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1202.95
293.15	0.0536	1185.47
293.15	0.1324	1160.15
293.15	0.1909	1141.63
293.15	0.2564	1121.18
293.15	0.3257	1099.86
293.15	0.3986	1077.76
293.15	0.4576	1060.12
293.15	0.5243	1040.42
293.15	0.5888	1021.61
293.15	0.6424	1006.13
293.15	0.7156	985.23
293.15	0.7756	968.27
293.15	0.8324	952.34
293.15	0.8755	940.34
293.15	0.9424	921.83
293.15	1.0000	906.0
303.15	0.0000	1193.56
303.15	0.0621	1173.19
303.15	0.1248	1152.93
303.15	0.1822	1134.64
303.15	0.2429	1115.56
303.15	0.3139	1093.59
303.15	0.3571	1080.39
303.15	0.4249	1059.93
303.15	0.4819	1042.96
303.15	0.5487	1023.33
303.15	0.5901	1011.29
303.15	0.6528	993.23
303.15	0.7289	971.58
303.15	0.7913	954.03
303.15	0.8592	935.12
303.15	0.9368	913.72
303.15	1.0000	896.44
313.15	0.0000	1183.37
313.15	0.0492	1167.15
313.15	0.1189	1144.52
313.15	0.1898	1121.9
313.15	0.2563	1101.03
313.15	0.3398	1075.31
313.15	0.4018	1056.54
313.15	0.4621	1038.54
313.15	0.5243	1020.21
313.15	0.5811	1003.69
313.15	0.6421	986.16
313.15	0.7132	965.98
313.15	0.7723	949.39
313.15	0.8421	930.01
313.15	0.8942	915.68
313.15	0.9524	899.79
313.15	1.0000	886.88
323.15	0.0000	1172.38
323.15	0.0598	1152.7
323.15	0.1329	1129.06
323.15	0.1942	1109.58
323.15	0.2458	1093.41
323.15	0.3239	1069.35
323.15	0.3891	1049.61
323.15	0.4314	1036.97
323.15	0.5028	1015.92
323.15	0.5622	998.67
323.15	0.6321	978.64
323.15	0.6873	963.03
323.15	0.7419	947.74
323.15	0.8054	930.15
323.15	0.8823	909.1
323.15	0.9339	895.1
323.15	1.0000	877.32
333.15	0.0000	1160.59
333.15	0.0647	1139.39
333.15	0.1278	1119.07
333.15	0.1825	1101.73
333.15	0.2542	1079.38
333.15	0.3183	1059.76
333.15	0.3798	1041.24
333.15	0.4248	1027.86
333.15	0.4892	1008.97
333.15	0.5329	996.32
333.15	0.5892	980.2
333.15	0.6379	966.41
333.15	0.7132	945.37
333.15	0.7987	921.85
333.15	0.8680	903.04
333.15	0.9468	881.9
333.15	1.0000	867.76
343.15	0.0000	1148.0
343.15	0.0687	1125.66
343.15	0.1139	1111.2
343.15	0.1842	1089.06
343.15	0.2389	1072.13
343.15	0.3234	1046.47
343.15	0.3894	1026.81
343.15	0.4346	1013.54
343.15	0.4903	997.4
343.15	0.5538	979.25
343.15	0.6140	962.29
343.15	0.6622	948.88
343.15	0.7319	929.71
343.15	0.7922	913.35
343.15	0.8531	896.99
343.15	0.9234	878.32
343.15	1.0000	858.2
353.15	0.0000	1134.61
353.15	0.0550	1116.88
353.15	0.1376	1090.79
353.15	0.1726	1079.91
353.15	0.2389	1059.6
353.15	0.3020	1040.61
353.15	0.3791	1017.85
353.15	0.4349	1001.66
353.15	0.5139	979.13
353.15	0.5628	965.4
353.15	0.6249	948.19
353.15	0.6733	934.94
353.15	0.7234	921.37
353.15	0.7981	901.38
353.15	0.8621	884.47
353.15	0.9412	863.83
353.15	1.0000	848.64

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Styrene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1202.95
293.15	0.0536	1185.47
293.15	0.1324	1160.15
293.15	0.1909	1141.63
293.15	0.2564	1121.18
293.15	0.3257	1099.86
293.15	0.3986	1077.76
293.15	0.4576	1060.12
293.15	0.5243	1040.42
293.15	0.5888	1021.61
293.15	0.6424	1006.13
293.15	0.7156	985.23
293.15	0.7756	968.27
293.15	0.8324	952.34
293.15	0.8755	940.34
293.15	0.9424	921.83
293.15	1.0000	906.0
303.15	0.0000	1193.56
303.15	0.0621	1173.19
303.15	0.1248	1152.93
303.15	0.1822	1134.64
303.15	0.2429	1115.56
303.15	0.3139	1093.59
303.15	0.3571	1080.39
303.15	0.4249	1059.93
303.15	0.4819	1042.96
303.15	0.5487	1023.33
303.15	0.5901	1011.29
303.15	0.6528	993.23
303.15	0.7289	971.58
303.15	0.7913	954.03
303.15	0.8592	935.12
303.15	0.9368	913.72
303.15	1.0000	896.44
313.15	0.0000	1183.37
313.15	0.0492	1167.15
313.15	0.1189	1144.52
313.15	0.1898	1121.9
313.15	0.2563	1101.03
313.15	0.3398	1075.31
313.15	0.4018	1056.54
313.15	0.4621	1038.54
313.15	0.5243	1020.21
313.15	0.5811	1003.69
313.15	0.6421	986.16
313.15	0.7132	965.98
313.15	0.7723	949.39
313.15	0.8421	930.01
313.15	0.8942	915.68
313.15	0.9524	899.79
313.15	1.0000	886.88
323.15	0.0000	1172.38
323.15	0.0598	1152.7
323.15	0.1329	1129.06
323.15	0.1942	1109.58
323.15	0.2458	1093.41
323.15	0.3239	1069.35
323.15	0.3891	1049.61
323.15	0.4314	1036.97
323.15	0.5028	1015.92
323.15	0.5622	998.67
323.15	0.6321	978.64
323.15	0.6873	963.03
323.15	0.7419	947.74
323.15	0.8054	930.15
323.15	0.8823	909.1
323.15	0.9339	895.1
323.15	1.0000	877.32
333.15	0.0000	1160.59
333.15	0.0647	1139.39
333.15	0.1278	1119.07
333.15	0.1825	1101.73
333.15	0.2542	1079.38
333.15	0.3183	1059.76
333.15	0.3798	1041.24
333.15	0.4248	1027.86
333.15	0.4892	1008.97
333.15	0.5329	996.32
333.15	0.5892	980.2
333.15	0.6379	966.41
333.15	0.7132	945.37
333.15	0.7987	921.85
333.15	0.8680	903.04
333.15	0.9468	881.9
333.15	1.0000	867.76
343.15	0.0000	1148.0
343.15	0.0687	1125.66
343.15	0.1139	1111.2
343.15	0.1842	1089.06
343.15	0.2389	1072.13
343.15	0.3234	1046.47
343.15	0.3894	1026.81
343.15	0.4346	1013.54
343.15	0.4903	997.4
343.15	0.5538	979.25
343.15	0.6140	962.29
343.15	0.6622	948.88
343.15	0.7319	929.71
343.15	0.7922	913.35
343.15	0.8531	896.99
343.15	0.9234	878.32
343.15	1.0000	858.2
353.15	0.0000	1134.61
353.15	0.0550	1116.88
353.15	0.1376	1090.79
353.15	0.1726	1079.91
353.15	0.2389	1059.6
353.15	0.3020	1040.61
353.15	0.3791	1017.85
353.15	0.4349	1001.66
353.15	0.5139	979.13
353.15	0.5628	965.4
353.15	0.6249	948.19
353.15	0.6733	934.94
353.15	0.7234	921.37
353.15	0.7981	901.38
353.15	0.8621	884.47
353.15	0.9412	863.83
353.15	1.0000	848.64

Sources

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