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dc.contributor.authorWagaarachchige, Jayangi Dinesha
dc.contributor.authorIdris, Zulkifli
dc.contributor.authorArstad, Bjørnar
dc.contributor.authorKummamuru, Nithin Bharadwaj
dc.contributor.authorSætre, Kai Arne
dc.contributor.authorHalstensen, Maths
dc.contributor.authorJens, Klaus-Joachim
dc.date.accessioned2022-10-26T07:14:56Z
dc.date.available2022-10-26T07:14:56Z
dc.date.created2022-09-22T10:52:17Z
dc.date.issued2022
dc.identifier.citationWagaarachchige, J. D., Idris, Z., Arstad, B., Kummamuru, N. B., Sætre, K. A. S., Halstensen, M. & Jens, K.-J. (2022). Low-Viscosity Nonaqueous Sulfolane–Amine–Methanol Solvent Blend for Reversible CO2 Capture. Industrial & Engineering Chemistry Research, 61(17), 5942-5951.en_US
dc.identifier.issn0888-5885
dc.identifier.urihttps://hdl.handle.net/11250/3028299
dc.description.abstractIn this work, the absorption–desorption performance of CO2 in six new solvent blends of amine (diisopropylamine (DPA), 2-amino-2-methyl-1-propanol (AMP), methyldiethanolamine (MDEA), diethanolamine (DEA), diisopropanolamine (DIPA), and ethanolamine (MEA)), sulfolane, and methanol has been monitored using ATR-FTIR spectroscopy. Additionally, NMR-based species confirmation and solvent viscosity analysis were done for DPA solvent samples. The identified CO2 capture products are monomethyl carbonate (MMC), carbamate, carbonate, and bicarbonate anions in different ratios. The DPA solvent formed MMC entirely with 0.88 molCO2/molamine capture capacity, 0.48 molCO2/molamine cyclic capacity, and 3.28 mPa·s CO2-loaded solvent viscosity. MEA, DEA, DIPA, and MDEA were shown to produce a low or a negligible amount of MMC while AMP occupied an intermediate position.en_US
dc.language.isoengen_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.titleLow-Viscosity Nonaqueous Sulfolane-Amine-Methanol Solvent Blend for Reversible CO2 Captureen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holder© 2022 The Authors. Published by American Chemical Society.en_US
dc.source.pagenumber5942-5951en_US
dc.source.volume61en_US
dc.source.journalIndustrial & Engineering Chemistry Researchen_US
dc.source.issue17en_US
dc.identifier.doihttps://doi.org/10.1021/acs.iecr.1c04946
dc.identifier.cristin2054239
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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