Mixture of Benzene, bromo- + Dimethyl Sulfoxide

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Benzene, bromo-

Name
Benzene, bromo-
InChI
InChI=1S/C6H5Br/c7-6-4-2-1-3-5-6/h1-5H
InChI Key
QARVLSVVCXYDNA-UHFFFAOYSA-N
Formula
C6H5Br
SMILES
Brc1ccccc1
Mol. Weight (g/mol)
157.01
CAS
108-86-1

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, bromo- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0325 0.0521
0.0701 0.1171
0.1122 0.1859
0.1574 0.2512
0.2039 0.3060
0.2518 0.3619
0.3014 0.4094
0.3485 0.4531
0.3767 0.4745
0.3955 0.4923
0.4091 0.4955
0.4468 0.5030
0.4960 0.5119
0.5567 0.5091
0.6277 0.4865
0.7077 0.4322
0.7985 0.3466
0.8979 0.2023

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

Operational conditions:

Mole fraction of Benzene, bromo- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0325 0.0521
0.0701 0.1171
0.1122 0.1859
0.1574 0.2512
0.2039 0.3060
0.2518 0.3619
0.3014 0.4094
0.3485 0.4531
0.3767 0.4745
0.3955 0.4923
0.4091 0.4955
0.4468 0.5030
0.4960 0.5119
0.5567 0.5091
0.6277 0.4865
0.7077 0.4322
0.7985 0.3466
0.8979 0.2023

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Benzene, bromo- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.1101 449.15
0.2198 441.05
0.3103 436.15
0.4521 430.75
0.6183 426.95
0.7297 425.45
0.8024 424.95
0.9012 424.65
1.0000 426.85

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Benzene, bromo- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.1101 449.15
0.2198 441.05
0.3103 436.15
0.4521 430.75
0.6183 426.95
0.7297 425.45
0.8024 424.95
0.9012 424.65
1.0000 426.85

Sources