Abstract

AbstractTo separate propylene from propane, whose boiling points are very close, leads to challenges, especially if it is intended to achieve higher energy efficiencies, reduce process expenses, and diminish environmental impacts. Polymer‐grade propylene can be obtained through an extractive distillation process, using 90 wt % of acetonitrile (ACN) as main solvent and 10 wt % of ethylenediamine (EDA) or methyl ethyl ketone or ethanol as co‐solvent, favoring the separation of propylene with purity greater than 99.60 mol % due to the increase of the relative volatility of propane. Compared to the use of aqueous N‐methyl‐2‐pyrrolidone (NMP) as extraction solvent, ACN‐EDA solvents have shown to be able to achieve savings of 8.09 % in total annual cost and 5.95 % in CO2 emissions. The results demonstrate that the extractive distillation process using ACN‐EDA can reduce process costs as well as CO2 emissions compared to the same process with aqueous NMP.

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