Mixture of Benzene, nitro- + Ethylbenzene

Excel

Benzene, nitro-

Name
Benzene, nitro-
InChI
InChI=1S/C6H5NO2/c8-7(9)6-4-2-1-3-5-6/h1-5H
InChI Key
LQNUZADURLCDLV-UHFFFAOYSA-N
Formula
C6H5NO2
SMILES
O=[N+]([O-])c1ccccc1
Mol. Weight (g/mol)
123.11
CAS
98-95-3

Ethylbenzene

Name
Ethylbenzene
InChI
InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3
InChI Key
YNQLUTRBYVCPMQ-UHFFFAOYSA-N
Formula
C8H10
SMILES
CCc1ccccc1
Mol. Weight (g/mol)
106.17
CAS
100-41-4
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. Tboil - 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 Ethylbenzene (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1202.95
293.15 0.0478 1184.56
293.15 0.1275 1154.51
293.15 0.1842 1133.58
293.15 0.2576 1107.04
293.15 0.3238 1083.6
293.15 0.4023 1056.42
293.15 0.4578 1037.57
293.15 0.5139 1018.83
293.15 0.5813 996.7
293.15 0.6423 977.03
293.15 0.6931 960.9
293.15 0.7592 940.24
293.15 0.8343 917.18
293.15 0.8824 902.65
293.15 0.9587 879.94
293.15 1.0000 867.82
303.15 0.0000 1193.56
303.15 0.0540 1172.67
303.15 0.1213 1147.16
303.15 0.1983 1118.67
303.15 0.2489 1100.34
303.15 0.3138 1077.25
303.15 0.3854 1052.32
303.15 0.4428 1032.74
303.15 0.5098 1010.3
303.15 0.5721 989.85
303.15 0.6219 973.76
303.15 0.6839 954.06
303.15 0.7429 935.62
303.15 0.8013 917.67
303.15 0.8632 898.94
303.15 0.9328 878.24
303.15 1.0000 858.6
313.15 0.0000 1183.37
313.15 0.0538 1162.71
313.15 0.1387 1130.89
313.15 0.1932 1110.93
313.15 0.2378 1094.87
313.15 0.2947 1074.72
313.15 0.3571 1053.04
313.15 0.4139 1033.68
313.15 0.4917 1007.73
313.15 0.5523 987.93
313.15 0.6139 968.18
313.15 0.6731 949.53
313.15 0.7248 933.5
313.15 0.7932 912.63
313.15 0.8536 894.54
313.15 0.9248 873.58
313.15 1.0000 851.85
323.15 0.0000 1172.38
323.15 0.0617 1149.22
323.15 0.1482 1117.58
323.15 0.2213 1091.54
323.15 0.2787 1071.53
323.15 0.3234 1056.2
323.15 0.3781 1037.74
323.15 0.4344 1019.07
323.15 0.4822 1003.47
323.15 0.5339 986.86
323.15 0.5920 968.49
323.15 0.6739 943.12
323.15 0.7429 922.2
323.15 0.8137 901.15
323.15 0.8735 883.68
323.15 0.9572 859.66
323.15 1.0000 847.58
333.15 0.0000 1160.59
333.15 0.0439 1144.65
333.15 0.1249 1115.84
333.15 0.1892 1093.51
333.15 0.2599 1069.48
333.15 0.3389 1043.25
333.15 0.4042 1022.06
333.15 0.4672 1002.01
333.15 0.5243 984.15
333.15 0.5902 963.91
333.15 0.6645 941.54
333.15 0.7309 921.93
333.15 0.8021 901.28
333.15 0.8623 884.12
333.15 0.8932 875.4
333.15 0.9621 856.21
333.15 1.0000 845.79
343.15 0.0000 1148.0
343.15 0.0535 1129.57
343.15 0.1122 1109.7
343.15 0.1834 1086.08
343.15 0.2478 1065.16
343.15 0.3044 1047.11
343.15 0.3782 1024.0
343.15 0.4519 1001.42
343.15 0.5130 983.04
343.15 0.5801 963.22
343.15 0.6529 942.11
343.15 0.7238 921.93
343.15 0.7932 902.5
343.15 0.8520 886.31
343.15 0.8932 875.09
343.15 0.9423 861.85
343.15 1.0000 846.48
353.15 0.0000 1134.61
353.15 0.0723 1111.4
353.15 0.1298 1093.3
353.15 0.1984 1072.07
353.15 0.2584 1053.83
353.15 0.3133 1037.4
353.15 0.3891 1015.12
353.15 0.4501 997.51
353.15 0.5240 976.53
353.15 0.5818 960.38
353.15 0.6630 938.08
353.15 0.7483 915.1
353.15 0.7964 902.32
353.15 0.8423 890.26
353.15 0.8893 878.02
353.15 0.9529 861.65
353.15 1.0000 849.64

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethylbenzene (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1202.95
293.15 0.0478 1184.56
293.15 0.1275 1154.51
293.15 0.1842 1133.58
293.15 0.2576 1107.04
293.15 0.3238 1083.6
293.15 0.4023 1056.42
293.15 0.4578 1037.57
293.15 0.5139 1018.83
293.15 0.5813 996.7
293.15 0.6423 977.03
293.15 0.6931 960.9
293.15 0.7592 940.24
293.15 0.8343 917.18
293.15 0.8824 902.65
293.15 0.9587 879.94
293.15 1.0000 867.82
303.15 0.0000 1193.56
303.15 0.0540 1172.67
303.15 0.1213 1147.16
303.15 0.1983 1118.67
303.15 0.2489 1100.34
303.15 0.3138 1077.25
303.15 0.3854 1052.32
303.15 0.4428 1032.74
303.15 0.5098 1010.3
303.15 0.5721 989.85
303.15 0.6219 973.76
303.15 0.6839 954.06
303.15 0.7429 935.62
303.15 0.8013 917.67
303.15 0.8632 898.94
303.15 0.9328 878.24
303.15 1.0000 858.6
313.15 0.0000 1183.37
313.15 0.0538 1162.71
313.15 0.1387 1130.89
313.15 0.1932 1110.93
313.15 0.2378 1094.87
313.15 0.2947 1074.72
313.15 0.3571 1053.04
313.15 0.4139 1033.68
313.15 0.4917 1007.73
313.15 0.5523 987.93
313.15 0.6139 968.18
313.15 0.6731 949.53
313.15 0.7248 933.5
313.15 0.7932 912.63
313.15 0.8536 894.54
313.15 0.9248 873.58
313.15 1.0000 851.85
323.15 0.0000 1172.38
323.15 0.0617 1149.22
323.15 0.1482 1117.58
323.15 0.2213 1091.54
323.15 0.2787 1071.53
323.15 0.3234 1056.2
323.15 0.3781 1037.74
323.15 0.4344 1019.07
323.15 0.4822 1003.47
323.15 0.5339 986.86
323.15 0.5920 968.49
323.15 0.6739 943.12
323.15 0.7429 922.2
323.15 0.8137 901.15
323.15 0.8735 883.68
323.15 0.9572 859.66
323.15 1.0000 847.58
333.15 0.0000 1160.59
333.15 0.0439 1144.65
333.15 0.1249 1115.84
333.15 0.1892 1093.51
333.15 0.2599 1069.48
333.15 0.3389 1043.25
333.15 0.4042 1022.06
333.15 0.4672 1002.01
333.15 0.5243 984.15
333.15 0.5902 963.91
333.15 0.6645 941.54
333.15 0.7309 921.93
333.15 0.8021 901.28
333.15 0.8623 884.12
333.15 0.8932 875.4
333.15 0.9621 856.21
333.15 1.0000 845.79
343.15 0.0000 1148.0
343.15 0.0535 1129.57
343.15 0.1122 1109.7
343.15 0.1834 1086.08
343.15 0.2478 1065.16
343.15 0.3044 1047.11
343.15 0.3782 1024.0
343.15 0.4519 1001.42
343.15 0.5130 983.04
343.15 0.5801 963.22
343.15 0.6529 942.11
343.15 0.7238 921.93
343.15 0.7932 902.5
343.15 0.8520 886.31
343.15 0.8932 875.09
343.15 0.9423 861.85
343.15 1.0000 846.48
353.15 0.0000 1134.61
353.15 0.0723 1111.4
353.15 0.1298 1093.3
353.15 0.1984 1072.07
353.15 0.2584 1053.83
353.15 0.3133 1037.4
353.15 0.3891 1015.12
353.15 0.4501 997.51
353.15 0.5240 976.53
353.15 0.5818 960.38
353.15 0.6630 938.08
353.15 0.7483 915.1
353.15 0.7964 902.32
353.15 0.8423 890.26
353.15 0.8893 878.02
353.15 0.9529 861.65
353.15 1.0000 849.64

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94.7 (Liquid)

Mole fraction of Ethylbenzene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 481.15
0.1225 462.65
0.3277 441.55
0.4105 435.25
0.6256 422.25
0.7148 417.95
0.8343 412.95
0.9093 410.15
1.0000 406.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94.7 (Liquid)

Mole fraction of Ethylbenzene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 481.15
0.1225 462.65
0.3277 441.55
0.4105 435.25
0.6256 422.25
0.7148 417.95
0.8343 412.95
0.9093 410.15
1.0000 406.95

Sources