Binary vapor-liquid phase equilibrium for carbon monoxide + hydrocarbons
Abstract
This study deals the binary vapor-liquid phase equilibrium for carbon monoxide in selected hydrocarbons. The solubilities of carbon monoxide in these hydrocarbons were measured at temperatures from 50�C to 160�C and pressures to 102 bar. Binary interaction parameters in the Soave-Redlich-Kwong equation and the Peng-Robinson equation were regressed from the experimental results for each of the systems studied; these equations provided excellent representation of the data.
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- OSU Theses [15752]