Mixture of Benzene, nitro- + Dimethyl Sulfoxide

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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

Dimethyl Sulfoxide

Name
Dimethyl Sulfoxide
InChI
InChI=1S/C2H6OS/c1-4(2)3/h1-2H3
InChI Key
IAZDPXIOMUYVGZ-UHFFFAOYSA-N
Formula
C2H6OS
SMILES
CS(C)=O
Mol. Weight (g/mol)
78.13
CAS
67-68-5
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Benzene, nitro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0935 0.0761
0.1856 0.1786
0.2722 0.2547
0.3514 0.3129
0.4247 0.3567
0.4887 0.3849
0.5445 0.4002
0.5600 0.4043
0.6061 0.3929
0.6576 0.3749
0.7072 0.3509
0.7577 0.3179
0.8125 0.2697
0.8647 0.2147
0.9154 0.1459
0.9624 0.0697

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Benzene, nitro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0935 0.0761
0.1856 0.1786
0.2722 0.2547
0.3514 0.3129
0.4247 0.3567
0.4887 0.3849
0.5445 0.4002
0.5600 0.4043
0.6061 0.3929
0.6576 0.3749
0.7072 0.3509
0.7577 0.3179
0.8125 0.2697
0.8647 0.2147
0.9154 0.1459
0.9624 0.0697

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Benzene, nitro- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.0725 458.15
0.1290 458.15
0.2568 459.25
0.3519 460.85
0.5465 465.35
0.6593 468.85
0.8289 475.05
0.9175 479.05
1.0000 483.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Benzene, nitro- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.0725 458.15
0.1290 458.15
0.2568 459.25
0.3519 460.85
0.5465 465.35
0.6593 468.85
0.8289 475.05
0.9175 479.05
1.0000 483.05

Sources