Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids

This paper presents a series of experimental and modelling studies on the thermodynamic inhibition effects of four ionic liquids on the methane hydrate formation. The investigated ionic liquids are 1-methyl-3-octylimidazolium chloride MOIM-Cl, 1-methylimidazolium hydrogen sulfate H-MIM-HSO4, tetraet...

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Main Authors: Nashed, O., Dadebayev, D., Khan, M.S., Bavoh, C.B., Lal, B., Shariff, A.M.
Format: Article
Published: Elsevier B.V. 2018
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85034868127&doi=10.1016%2fj.molliq.2017.11.115&partnerID=40&md5=f34f643bb367e1f0c5272471e605baaf
http://eprints.utp.edu.my/21903/
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spelling my.utp.eprints.219032019-01-10T06:47:56Z Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids Nashed, O. Dadebayev, D. Khan, M.S. Bavoh, C.B. Lal, B. Shariff, A.M. This paper presents a series of experimental and modelling studies on the thermodynamic inhibition effects of four ionic liquids on the methane hydrate formation. The investigated ionic liquids are 1-methyl-3-octylimidazolium chloride MOIM-Cl, 1-methylimidazolium hydrogen sulfate H-MIM-HSO4, tetraethylammonium iodide TEA-I, and 1-hexyl-3-methylimidazolium iodide HMIM-I. The impact of 0.1 mass fraction concentration ionic liquids on the methane hydrate phase boundary was evaluated by measuring the dissociation temperature of methane hydrate in the pressure range of 5.1�11.1 MPa, using a high pressure differential scanning calorimeter. The molar dissociation enthalpy of methane hydrates was calculated using the Clausius�Clapeyron equation. The density was measured for 0.10 mass fraction of aqueous solutions of ionic liquids at 293.15 K, and then compared to the commercially available gas hydrate inhibitors. The results demonstrated that 1-methylimidazolium hydrogen sulfate H-MIM-HSO4 has the highest inhibitory performance among the four ionic liquids considered. Moreover, the Dickens and Quinby-Hunt (electrolyte) model was applied to predict the phase equilibrium data of the studied ILs. The predicted data is in agreement with the experimental data. © 2017 Elsevier B.V. 2018 Article PeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-85034868127&doi=10.1016%2fj.molliq.2017.11.115&partnerID=40&md5=f34f643bb367e1f0c5272471e605baaf Nashed, O. and Dadebayev, D. and Khan, M.S. and Bavoh, C.B. and Lal, B. and Shariff, A.M. (2018) Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids. Journal of Molecular Liquids, 249 . pp. 886-891. http://eprints.utp.edu.my/21903/
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
description This paper presents a series of experimental and modelling studies on the thermodynamic inhibition effects of four ionic liquids on the methane hydrate formation. The investigated ionic liquids are 1-methyl-3-octylimidazolium chloride MOIM-Cl, 1-methylimidazolium hydrogen sulfate H-MIM-HSO4, tetraethylammonium iodide TEA-I, and 1-hexyl-3-methylimidazolium iodide HMIM-I. The impact of 0.1 mass fraction concentration ionic liquids on the methane hydrate phase boundary was evaluated by measuring the dissociation temperature of methane hydrate in the pressure range of 5.1�11.1 MPa, using a high pressure differential scanning calorimeter. The molar dissociation enthalpy of methane hydrates was calculated using the Clausius�Clapeyron equation. The density was measured for 0.10 mass fraction of aqueous solutions of ionic liquids at 293.15 K, and then compared to the commercially available gas hydrate inhibitors. The results demonstrated that 1-methylimidazolium hydrogen sulfate H-MIM-HSO4 has the highest inhibitory performance among the four ionic liquids considered. Moreover, the Dickens and Quinby-Hunt (electrolyte) model was applied to predict the phase equilibrium data of the studied ILs. The predicted data is in agreement with the experimental data. © 2017
format Article
author Nashed, O.
Dadebayev, D.
Khan, M.S.
Bavoh, C.B.
Lal, B.
Shariff, A.M.
spellingShingle Nashed, O.
Dadebayev, D.
Khan, M.S.
Bavoh, C.B.
Lal, B.
Shariff, A.M.
Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
author_facet Nashed, O.
Dadebayev, D.
Khan, M.S.
Bavoh, C.B.
Lal, B.
Shariff, A.M.
author_sort Nashed, O.
title Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
title_short Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
title_full Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
title_fullStr Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
title_full_unstemmed Experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
title_sort experimental and modelling studies on thermodynamic methane hydrate inhibition in the presence of ionic liquids
publisher Elsevier B.V.
publishDate 2018
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85034868127&doi=10.1016%2fj.molliq.2017.11.115&partnerID=40&md5=f34f643bb367e1f0c5272471e605baaf
http://eprints.utp.edu.my/21903/
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