Bubble-Point
Measurements of <i>n</i>‑Butane + <i>n</i>‑Octane and <i>n</i>‑Butane + <i>n-</i>Nonane Binary Mixtures
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Abstract
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