Binary Vapor-liquid Phase Equilibrium for Methane and Carbon Monoxide in Selected Hydrocarbons�
Abstract
This study details the binary vapor-liquid phase equilibrium for methane and carbon monoxide in selected hydrocarbons. The solubilities of methane and carbon monoxide were measured at temperatures from 104 to 302 �F and pressures to 104 bar in selected hydrocarbons. Binary interaction parameters have been obtained using the SoaveRedlich- Kwong and Peng-Robinson equations of state for each of the systems studied.
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- OSU Theses [15752]