Removal of small hydrocarbons (ethane, propane, butane) from natural gas streams using the ionic liquid 1-ethyl-3 -methylimidazolium tris(pentafluoroethyl)trifluorophosphate

  • Mamoun Althuluth
  • , Maria Teresa Mota-Martinez
  • , Abdallah Berrouk
  • , Maaike C. Kroon
  • , Cor J. Peters

Research output: Contribution to journalArticlepeer-review

30 Scopus citations

Abstract

From our earlier work it was found that the ionic liquid (IL) 1-ethyl-3-methylimidazolium tris(pentafluoroethyl)trifluorophosphate ([emim][FAP]) shows a very high carbon dioxide (CO2) solubility and a low methane (CH4) solubility, with the consequence that this ionic liquid has a high CO2/CH4 selectivity (M. Althuluth, M.C. Kroon, C.J. Peters, Ind. Eng. Chem. Res., 2012, (51), pp 16709-16712). In this paper we measure for the first time the absorption capacity in the same IL of other small hydrocarbons, e.g. ethane (C2H6), propane (C3H8) and butane (C4H10). The solubility of these hydrocarbons in [emim][FAP] has been determined as a function of temperature and concentration by measuring bubble points and cloud points in a temperature window of 290-365 K and at pressures up to 10 MPa, using a synthetic method. It was observed that at similar conditions the solubility decreases in the following order: C4H10 > CO 2 > C3H8 > C2H6 > CH4. Maximum selectivities for CO2/hydrocarbon separations are established at the lowest temperatures. A comparison of the absorption enthalpies of the various hydrocarbons studied in this work showed that C4H10 has the highest value (Δhabs).

Original languageBritish English
Pages (from-to)65-72
Number of pages8
JournalJournal of Supercritical Fluids
Volume90
DOIs
StatePublished - Jun 2014

Keywords

  • Carbon Dioxide
  • Gas separation
  • Hydrocarbons
  • Ionic liquid
  • Liquid-liquid immiscibility
  • Phase behavior

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