Multicomponent vapor-liquid equilibria measurements for the development of an extractive distillation process for the processing of gas issuing from a CO2 enhanced oil recovery project

Abstract

This paper provides vapor-liquid equilibria data for the design of the upper section of the all-important column treating the stabilized feed gas from C02 enhanced oil recovery (EOR) projects. Again, the extractive agent is represented by n-pentane. The simulated feed gas containing the methane,