Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K

Verma, N.[Naveen], Maken, S.[Sanjeev], Deshwal, B. R.[Bal Raj], Singh, K. C.[Krishan Chander], Park, J.-W.[Jin-Won]
J. Chem. Eng. Data 2007, 52, 5, 2083-2085
ABSTRACT
The molar excess volumes (VE) of sec-butyl chloride or tert-butyl chloride (A) + benzene or toluene or o- or m- or p-xylene (B) were measured at T = 298.15 K over the entire composition range using a V-shaped dilatometer. The VE values for all these binary mixtures were found to be negative, whereas these change sign from positive to negative for sec-butyl chloride + benzene. Although the VE values for an equimolar mixture of sec-butyl chloride + aromatics vary in the order benzene greater than m-xylene greater than toluene greater than p-xylene greater than o-xylene, for an equimolar mixture of tert-butyl chloride + aromatics, these follow the sequence benzene greater than m-xylene greater than p-xylene greater than toluene greater than o-xylene. Branching of the butyl group decreases the VE in the following order: n-butyl chloride greater than sec-butyl chloride greater than tert-butyl chloride
Compounds
# Formula Name
1 C4H9Cl 2-chlorobutane
2 C4H9Cl 2-chloro-2-methylpropane
3 C6H6 benzene
4 C7H8 toluene
5 C8H10 1,2-dimethylbenzene
6 C8H10 1,4-dimethylbenzene
7 C8H10 1,3-dimethylbenzene
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 3
  • 1
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 16
  • POMD
  • 1
  • 4
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 12
  • POMD
  • 1
  • 5
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 14
  • POMD
  • 1
  • 6
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 13
  • POMD
  • 1
  • 7
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 13
  • POMD
  • 3
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 13
  • POMD
  • 4
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 15
  • POMD
  • 5
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 14
  • POMD
  • 6
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 13
  • POMD
  • 7
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • DIRDIL:UFactor:4
  • 13