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<dc:title>Solubility measurements of carbon dioxide and nitrous oxide in an aqueous mixture of 2-dimethylaminoethanol and N-methyl-1,3-propanediamine</dc:title>
<dc:creator>Arroyave Roa, Juan Diego</dc:creator>
<dc:creator>Moreau Ortega, Alejandro</dc:creator>
<dc:creator>Paredes Mendez, Xavier</dc:creator>
<dc:creator>Velez Jaramillo, Jhon Fredy</dc:creator>
<dc:creator>Martín Trusler, J.P.</dc:creator>
<dc:creator>Martín González, María del Carmen</dc:creator>
<dc:subject>CO2 capture</dc:subject>
<dc:subject>Amine blends</dc:subject>
<dc:subject>DMAE</dc:subject>
<dc:subject>MAPA</dc:subject>
<dc:subject>Vapour-liquid equilibrium</dc:subject>
<dc:subject>Solubility</dc:subject>
<dc:subject>33 Ciencias Tecnológicas</dc:subject>
<dc:description>Producción Científica</dc:description>
<dc:description>Aqueous monoethanolamine (MEA) is a mature post-combustion CO2 capture technology, but it faces significant drawbacks including corrosivity, high regeneration energy (∼4 GJ/t-CO2), and reactivity with contaminants. This study investigates an aqueous blend of 2-Dimethylaminoethanol (DMAE, 30% wt.) and N-Methyl-1,3-propanediamine (MAPA, 10% wt.) as an alternative solvent to capture CO2. Given the scarcity of Vapour-Liquid Equilibrium (VLE) data for such amine blends, this research aims to expand the thermodynamic understanding of this specific aqueous DMAE + MAPA system. We thoroughly investigate its VLE with CO2 and N2O across temperatures between (313.15–393.15) K. The physical solubility of CO2 was determined using the N2O/CO2 analogy. N2O solubility measurements were conducted in a monobloc equilibrium cell from 1 to 5 MPa. The expanded relative uncertainty of the N2O solubility, expressed in molality, was estimated to be 0.8% (k = 2). Henry's constants were derived using Krichevsky-Ilinskaya analysis and CO2 solubility was determined using a static-isochoric Van Ness-type apparatus over 313.15–363.15 K and up to 7 MPa with a relative uncertainty of ur(αexp) = (0.3–5) %. Finally, speciation profiles and the heat of CO2 absorption were predicted using established thermodynamic models optimized for this system.</dc:description>
<dc:description>Ministerio de Ciencia e Innovación - MICIU/AEI/10.13039/501100011033 y por FEDER/UE (subvención PID2021-125749OB-I00)</dc:description>
<dc:description>Junta de Castilla Leon (Consejería de Educación) y de los Fondos FEDER (Referencia: CLU-2025-2-05)</dc:description>
<dc:date>2026-04-07T12:32:36Z</dc:date>
<dc:date>2026-04-07T12:32:36Z</dc:date>
<dc:date>2026</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
<dc:identifier>The Journal of Chemical Thermodynamics, 2026, vol. 217, p. 107675</dc:identifier>
<dc:identifier>0021-9614</dc:identifier>
<dc:identifier>https://uvadoc.uva.es/handle/10324/83945</dc:identifier>
<dc:identifier>10.1016/j.jct.2026.107675</dc:identifier>
<dc:identifier>107675</dc:identifier>
<dc:identifier>The Journal of Chemical Thermodynamics</dc:identifier>
<dc:identifier>217</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>https://www.sciencedirect.com/science/article/pii/S0021961426000522</dc:relation>
<dc:rights>Atribución 4.0 Internacional</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by/4.0/</dc:rights>
<dc:rights>© 2026 The Author(s)</dc:rights>
<dc:format>application/pdf</dc:format>
<dc:publisher>Elsevier</dc:publisher>
<europeana:object>https://uvadoc.uva.es/bitstream/10324/83945/4/Solubility-measurements-carbon-dioxide.pdf.jpg</europeana:object>
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<europeana:type>TEXT</europeana:type>
<europeana:rights>http://creativecommons.org/licenses/by/4.0/</europeana:rights>
<europeana:dataProvider>UVaDOC. Repositorio Documental de la Universidad de Valladolid</europeana:dataProvider>
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