Three-Phase Equilibria of CO2 Hydrate from Computer Simulation in the Presence of NaCl

dc.contributor.authorBorrero Olea, Antonio
dc.contributor.authorDíaz Acosta, Adrián
dc.contributor.authorBlázquez, Samuel
dc.contributor.authorZerón, Iván M.
dc.contributor.authorAlgaba Fernández, Jesús
dc.contributor.authorMartín Conde, María
dc.contributor.authorJiménez Blas, Felipe
dc.date.accessioned2026-01-09T12:01:22Z
dc.date.available2026-01-09T12:01:22Z
dc.date.issued2025-03-10
dc.description.abstractIn this work, the cryoscopic decrease effect, as a function of the NaCl concentration, on the carbon dioxide (CO2) hydrate dissociation line conditions was determined through molecular dynamic simulations. In particular, we have determined the three-phase (solid hydrate–aqueous phase–liquid CO2) coexistence temperature at 100, 400, and 1000 bar at several initial NaCl concentrations in the aqueous phase, from 0.0 to 3.0 m, using the direct-coexistence technique. We used the well-known TIP4P/2005 and TraPPe force fields for water and CO2 molecules, respectively. Also, the water–salt interactions were described using the Madrid-2019 force field, which has been specifically developed for various salts in combination with the TIP4P/2005 water model. According to the results obtained in this work, the dissociation temperature of the CO2 hydrate decreases when the NaCl concentration in the initial aqueous phase increases. The results obtained are in excellent agreement with the experimental data reported in the literature. We have also observed how the dynamics of melting and growth of the CO2 hydrate becomes slower when the NaCl concentration is increased. As a consequence, longer simulation times (on the order of dozens of microseconds) are necessary when the NaCl concentration increases. Finally, we have also analyzed finite-size effects on the three-phase coexistence temperature of these systems by performing simulations at 400 bar with two different system sizes at two different NaCl concentrations (0.0 and 3.0 m). Non-negligible deviations have been found between the results obtained from the two system sizes.
dc.description.centerCIQSO
dc.description.departmentCiencias Integradas
dc.description.sponsorshipMinisterio de Ciencia e Innovación (Grant Nos. PID2021-125081NB-I00 and PID2022-136919NB-C32), Junta de Andalucía (P20-00363), and Universidad de Huelva (P.O. FEDER UHU-1255522, FEDER-UHU-202034, and EPIT1282023)
dc.identifier.citationBorrero, A., Díaz-Acosta, A., Blazquez, S., Zerón, I. M., Algaba, J., Conde, M. M., & Blas, F. J. (2025). Three-Phase Equilibria of CO2 Hydrate from Computer Simulation in the Presence of NaCl. Energy & Fuels, 39(11), 5522-5533. https://doi.org/10.1021/acs.energyfuels.5c00174
dc.identifier.doi10.1021/acs.energyfuels.5c00174
dc.identifier.issn0887-0624
dc.identifier.urihttps://hdl.handle.net/10272/27616
dc.language.isoeng
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internationalen
dc.rights.accessRightsopen access
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/
dc.subjectDissociation
dc.subjectMolecules
dc.subjectSolution chemistry
dc.subjectSolvates
dc.subjectWater
dc.titleThree-Phase Equilibria of CO2 Hydrate from Computer Simulation in the Presence of NaCl
dc.title.alternativeEquilibrio trifásico del hidrato de CO2 mediante simulación por ordenador en presencia de NaCl
dc.typejournal article
dc.type.hasVersionVoR
dspace.entity.typePublication
relation.isAuthorOfPublicationb41a1f9f-0ff0-45eb-90bd-d8d36f3b6c29
relation.isAuthorOfPublication0e2817b8-61ac-4619-a7e7-1563cbef26ed
relation.isAuthorOfPublication5fbe9948-210f-4a30-a57a-3638ef025f06
relation.isAuthorOfPublication.latestForDiscovery5fbe9948-210f-4a30-a57a-3638ef025f06

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