Mixture of Benzene, nitro- + Butane, 1-bromo-

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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

Butane, 1-bromo-

Name
Butane, 1-bromo-
InChI
InChI=1S/C4H9Br/c1-2-3-4-5/h2-4H2,1H3
InChI Key
MPPPKRYCTPRNTB-UHFFFAOYSA-N
Formula
C4H9Br
SMILES
CCCCBr
Mol. Weight (g/mol)
137.02
CAS
109-65-9
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, nitro- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.1230 0.0007
293.15 0.2445 0.0008
293.15 0.3645 0.0009
293.15 0.4240 0.0010
293.15 0.5420 0.0011
293.15 0.6585 0.0013
293.15 0.7737 0.0015
293.15 0.8875 0.0017
293.15 0.9439 0.0018
298.15 0.1230 0.0007
298.15 0.2445 0.0008
298.15 0.3645 0.0009
298.15 0.4240 0.0009
298.15 0.5420 0.0011
298.15 0.6585 0.0012
298.15 0.7737 0.0014
298.15 0.8875 0.0016
298.15 0.9439 0.0017
303.15 0.1230 0.0006
303.15 0.2445 0.0007
303.15 0.3645 0.0008
303.15 0.4240 0.0009
303.15 0.5420 0.0010
303.15 0.6585 0.0011
303.15 0.7737 0.0013
303.15 0.8875 0.0014
303.15 0.9439 0.0015
308.15 0.1230 0.0006
308.15 0.2445 0.0007
308.15 0.3645 0.0008
308.15 0.4240 0.0008
308.15 0.5420 0.0009
308.15 0.6585 0.0010
308.15 0.7737 0.0012
308.15 0.8875 0.0013
308.15 0.9439 0.0014

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, nitro- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.1230 0.0007
293.15 0.2445 0.0008
293.15 0.3645 0.0009
293.15 0.4240 0.0010
293.15 0.5420 0.0011
293.15 0.6585 0.0013
293.15 0.7737 0.0015
293.15 0.8875 0.0017
293.15 0.9439 0.0018
298.15 0.1230 0.0007
298.15 0.2445 0.0008
298.15 0.3645 0.0009
298.15 0.4240 0.0009
298.15 0.5420 0.0011
298.15 0.6585 0.0012
298.15 0.7737 0.0014
298.15 0.8875 0.0016
298.15 0.9439 0.0017
303.15 0.1230 0.0006
303.15 0.2445 0.0007
303.15 0.3645 0.0008
303.15 0.4240 0.0009
303.15 0.5420 0.0010
303.15 0.6585 0.0011
303.15 0.7737 0.0013
303.15 0.8875 0.0014
303.15 0.9439 0.0015
308.15 0.1230 0.0006
308.15 0.2445 0.0007
308.15 0.3645 0.0008
308.15 0.4240 0.0008
308.15 0.5420 0.0009
308.15 0.6585 0.0010
308.15 0.7737 0.0012
308.15 0.8875 0.0013
308.15 0.9439 0.0014

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, nitro- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.1230 1270.9
293.15 0.2445 1262.8
293.15 0.3645 1253.7
293.15 0.4240 1249.7
293.15 0.5420 1240.8
293.15 0.6585 1229.4
293.15 0.7737 1220.6
293.15 0.8875 1211.5
293.15 0.9439 1206.7
298.15 0.1230 1263.5
298.15 0.2445 1256.6
298.15 0.3645 1247.1
298.15 0.4240 1244.0
298.15 0.5420 1234.4
298.15 0.6585 1223.8
298.15 0.7737 1214.7
298.15 0.8875 1206.6
298.15 0.9439 1201.6
303.15 0.1230 1256.5
303.15 0.2445 1249.8
303.15 0.3645 1240.8
303.15 0.4240 1238.0
303.15 0.5420 1228.2
303.15 0.6585 1218.5
303.15 0.7737 1209.9
303.15 0.8875 1201.6
303.15 0.9439 1196.5
308.15 0.1230 1249.0
308.15 0.2445 1242.4
308.15 0.3645 1234.3
308.15 0.4240 1230.7
308.15 0.5420 1222.2
308.15 0.6585 1212.4
308.15 0.7737 1205.1
308.15 0.8875 1196.0
308.15 0.9439 1191.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, nitro- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.1230 1270.9
293.15 0.2445 1262.8
293.15 0.3645 1253.7
293.15 0.4240 1249.7
293.15 0.5420 1240.8
293.15 0.6585 1229.4
293.15 0.7737 1220.6
293.15 0.8875 1211.5
293.15 0.9439 1206.7
298.15 0.1230 1263.5
298.15 0.2445 1256.6
298.15 0.3645 1247.1
298.15 0.4240 1244.0
298.15 0.5420 1234.4
298.15 0.6585 1223.8
298.15 0.7737 1214.7
298.15 0.8875 1206.6
298.15 0.9439 1201.6
303.15 0.1230 1256.5
303.15 0.2445 1249.8
303.15 0.3645 1240.8
303.15 0.4240 1238.0
303.15 0.5420 1228.2
303.15 0.6585 1218.5
303.15 0.7737 1209.9
303.15 0.8875 1201.6
303.15 0.9439 1196.5
308.15 0.1230 1249.0
308.15 0.2445 1242.4
308.15 0.3645 1234.3
308.15 0.4240 1230.7
308.15 0.5420 1222.2
308.15 0.6585 1212.4
308.15 0.7737 1205.1
308.15 0.8875 1196.0
308.15 0.9439 1191.2

Sources