Thermodynamics Research Center / ThermoML | Thermochimica Acta

Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component

Siitsman, C.[Carmen], Oja, V.[Vahur]
Thermochim. Acta 2016, 637, 24-30
ABSTRACT
This study is aimed to extend an application of the differential scanning calorimeter (DSC) based vaporpressure method to evaluate vaporization of a target substance from a complex matrix that exhibits sev-eral times lower vapor pressure. The experiments involved preparing mixtures of known composition andmeasuring their vapor pressure by a DSC based vapor pressure method (following ASTM 1785 guidelines).The vapor pressure of two types of associating binary systems were examined: (1) a narrow boilingrange oil fraction (or distillation cut) mixed with a pure compound (nicotine or 2-tert-butylphenol); (2)a mixture of two narrow boiling range oil fractions. Emphasis was placed on 50:50 mol% mixtures. Toevaluate deviation from ideality, the total vapor pressure curves measured were compared to valuescalculated from Raoult s law. Narrow boiling range oil fractions (distillation cuts) were treated as singlepseudocomponents in these calculations. The vapor pressure curves obtained suggest that the DSC basedvapor pressure method is a useful tool for characterizing these kinds of multicomponent systems. Theresults presented can be viewed as a preliminary indication of the extent of ideality in systems containing synthetic crude oil from Kukersite oil shale, which is rich in alkyl-phenolic moieties.
Compounds
# Formula Name
1 C10H14O 2-tert-butyl-1-hydroxybenzene
2 C6H6 benzene
3 C7H8 toluene
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
  • 1
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • DSC
  • 5
  • POMD
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • DSC
  • 5
  • POMD
  • 2
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • DSC
  • 5