abstract

• To 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 %25 of acetonitrile (ACN) as main solvent and 10 wt %25 of ethylenediamine (EDA) or methyl ethyl ketone or ethanol as co-solvent, favoring the separation of propylene with purity greater than 99.60 mol %25 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 %25 in total annual cost and 5.95 %25 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. © 2022 Wiley-VCH GmbH.

authors

• González-Alatorre G.
• Louvier-Hernández J.F.
• Patiño-Herrera R.

publication date

• 2022-01-01

funding provided via

• Tecnológico Nacional de México, TNM  Grant

published in

• Chemical Engineering and Technology  Journal

keywords

• CO2 emission; Extractive distillation process; Process costs; Propylene; Separating agents Carbon dioxide; Distillation; Energy efficiency; Environmental impact; Ketones; Organic solvents; Propane; CO 2 emission; Distillation process; Ethylene diamine; Extractive distillation; Extractive distillation process; High energy efficiency; N-methyl-2-pyrrolidone; Polymer-grade propylene; Process costs; Separating agents; Propylene

Digital Object Identifier (DOI)

• 10.1002/ceat.202200110

PubMed ID

start page

• 1571

end page

• 1580

volume

• 45

issue

• 9