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

Viscosity and Density of Normal Butane Simultaneously Measured at Temperatures from (298 to 448) K and at Pressures up to 30 MPa Incorporating the Near-Critical Region

Herrmann, S.[Sebastian], Vogel, E.[Eckhard]
J. Chem. Eng. Data 2015, 60, 12, 3703-3720
ABSTRACT
A vibrating-wire viscometer and a single-sinker densimeter were simultaneously used to determine accurate ??pT data for normal butane. Seven isotherms were measured between (298.15 and 448.15) K up to maxima of 91 % of the saturated vapor pressure for the subcritical and of 30 MPa for the supercritical isotherms. The combined expanded uncertainty (k = 2) in density is 0.2 %, except for the low-density region. The data agree within +-0.4 % with densities for the equation of state by Bucker and Wagner, excluding the near-critical region due to the strong influence of allocation errors for temperature and pressure. The deviations for the near-critical isotherm 428.15 K amount to +8.5 %, distinctly higher than the total expanded uncertainty of the density data (2.4 %). The viscosity measurement is less influenced in the near-critical region by allocation errors for temperature and density so that the total expanded uncertainty is 0.6 %. The new data were compared with viscosity correlations of Younglove and Ely, Vogel et al., and Quinones-Cisneros and Deiters. Maximum deviations between +16 % and -7 % at 428.15 K and densities 150 less than ?/kg*m 3 less than 300 exceed seriously the expanded uncertainties of 6.0 % for the three correlations. The effect of about +1 % for the critical enhancement is obvious for 428.15 K. The present data should be used to generate a new viscosity correlation.
Compounds
# Formula Name
1 C4H10 butane
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
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Buoyancy - hydrostatic balance with magnetic suspension - one sinker
  • 295
  • POMD
  • 1
  • Viscosity, Pa*s ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Vibrating wire viscometry
  • 295