2 research outputs found
Bubble-Point Measurements of <i>n</i>‑Butane + <i>n</i>‑Octane and <i>n</i>‑Butane + <i>n-</i>Nonane Binary Mixtures
Mixtures of small gaseous hydrocarbons
with longer chain hydrocarbons
are of interest to the natural gas industry as well as other industries
in which separations are critical. In particular, binary mixtures
of <i>n-</i>nonane are of interest, because <i>n-</i>nonane was recently incorporated into the GERG-2008 equation of state,
but there is little experimental vapor–liquid equilibrium (VLE)
data available to support the equation. The bubble-point pressures
of four compositions of each of the binary mixtures <i>n</i>-butane + <i>n</i>-octane and <i>n</i>-butane
+ <i>n-</i>nonane were measured over the temperature range
of 270 to 370 K. The data and the expanded uncertainty (at a 95 % confidence
level, <i>k</i> = 2) of each point are reported. Additionally,
the data are compared to existing literature data for the <i>n-</i>butane + <i>n</i>-octane and the GERG-2008 equation
for both systems. This is the first report of vapor–liquid
equilibrium measurements on <i>n</i>-butane + <i>n-</i>nonane binary mixtures
Bubble-Point Measurements of <i>n</i>‑Propane + <i>n</i>‑Decane Binary Mixtures with Comparisons of Binary Mixture Interaction Parameters for Linear Alkanes
To
develop comprehensive models for multicomponent natural gas
mixtures, it is necessary to have binary interaction parameters for
each of the pairs of constituent fluids that form the mixture. The
determination of accurate mixture interaction parameters depends on
reliably collected experimental data. In this work, we have carried
out an experimental campaign to measure the bubble-point pressures
of mixtures of <i>n</i>-propane and <i>n</i>-decane,
a mixture that has been thus far poorly studied with only four existing
data sets. The experimental measurements of bubble-point states span
a composition range (in <i>n</i>-propane mole fraction)
from 0.148 to 0.731, and the bubble-point pressures are measured in
the temperature range from 270 to 370 K. These data, in conjunction
with data from a previous publication on mixtures of <i>n</i>-butane + <i>n</i>-octane and <i>n</i>-butane
+ <i>n</i>-nonane, are used to determine binary interaction
parameters. The newly obtained binary interaction parameters for the
mixture of <i>n</i>-propane and <i>n</i>-decane
represent the experimental bubble-point pressures given here to within
8% (coverage factor, <i>k</i> = 2), as opposed to previous
deviations up to 19%