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

Shear Viscosities of Methycyclohexane, Perfluoromethylcyclohexane, and Their Mixtures in the Vicinity of the Upper Critical Mixing Temperature. 1. Critical Isopleth and Coexistence Curve

Davies, M. K.[Michael K.], Archer, A. L.[Amanda L.], Maczek, A. O. S.[Andrew O. S.], Manzanares-Papayanopoulos, E.[Emilio], McLure, I. A.[Ian A.]
J. Chem. Eng. Data 2006, 51, 5, 1502-1508
ABSTRACT
Shear viscosities e are reported for pure liquid methylcyclohexane (MCH) from 298.610 K to 333.694 K, for perfluoromethylcyclohexane (PFMCH) from 319.196 K to 333.114 K and for a MCH + PFMCH mixture of overall PFMCH near-critical mole fraction, xc ) 0.3640, from (TUCS/K - 7) in the region of biphase liquid coexistence to (TUCS/K + 20) in the uniphase region, where TUCS ) 320.13 K is the air-saturated upper liquidliquid critical solution temperature. The measurements were made using a capillary rheometer that permits the measurement of the viscosity of thermally equilibrated coexisting-liquid phases. The results confirm that the near-critical viscosity exhibits a weak enhancement that strictly speaking becomes a divergence when account is taken of the finite shear gradients in the capillary during measurements. The viscosity of the uniphase mixture of critical composition is well-described after shear gradient correction by a multiplicative combination of an Arrhenius background and a critical power expression with an index close to the now-accepted universal value y ) 0.0435. The chief objective of the work, in addition to contributing to knowledge of this aspect of near-critical rheology, is the development for the biphase of a simple expression for the temperature dependence of the viscosities of the coexisting phases, e+ and e-, that combines (a) an expression for the viscosity diameter less thanegreater than ) 1/2(e+ + e-) similar to that for the viscosity of the critical mixture in the uniphase region, with a similar best critical index ycents between 0.041 and 0.0435, and (b) an expression for centse ) (e+ - e-) that behaves like an order parameter, with an index a very close to the normal value a ) 0.325 and as many Wegner correction terms as the data require. The best two-phase fit emerges from a freely fitted exponent ycents 0.037 with one Wegner-extended scaling term, but we believe that were shear gradient correction to be applied, the best ycents would be the consensus value ycents ) 0.0435. The magnitude of ycents notwithstanding, we believe that our primary objective has been satisfied, namely, the formulation of an expression that affords a good description of the shear and background viscosities of nearcritical mixtures in the one- and two-liquid phases in relation to our estimates of the nano- or molecular-viscosity derived from measurements of fluorescence polarization decay rates.
Compounds
# Formula Name
1 C7H14 methylcyclohexane
2 C7F14 perfluoro(methylcyclohexane)
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
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 7
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 5
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 20
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • Capillary tube (Ostwald; Ubbelohde) method
  • 8
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • Capillary tube (Ostwald; Ubbelohde) method
  • 9