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dc.contributor.authorSantamaría, Diego
dc.contributor.authorHernández Blázquez, Borja 
dc.contributor.authorMartín Martín, Mariano 
dc.date.accessioned2024-03-13T11:51:48Z
dc.date.available2024-03-13T11:51:48Z
dc.date.issued2023
dc.identifier.citationDiego Santamaría, Borja Hernández, and Mariano Martín ACS Sustainable Chemistry & Engineering 2023 11 (31), 11502-11515 DOI: 10.1021/acssuschemeng.3c01627es_ES
dc.identifier.issn2168-0485
dc.identifier.urihttp://hdl.handle.net/10366/156565
dc.description.abstract[EN]This work provides an economic and environmental comparison of two processes (direct chlorination of methane and hydrochlorination of methanol) to produce chloromethanes from waste brine and CO2. Both processes are modeled using an equation-based approach. This allows for determining the optimal operating conditions of all of the units involved in the process. In particular, those related to the reactors. The optimization determines that hydrochlorination of methanol is a more profitable process (a minimum selling price of $1.8/kgmethyl chloride) than direct chlorination (∼$5/kgmethyl chloride) since the conversion achieved in hydrochlorination is approximately 5 times greater, although the desired product among all of the chloromethanes in direct chlorination is also methyl chloride. Furthermore, direct hydrochlorination also has higher emissions, 16.2 kgCO2/kgmethyl chloride vs 4.6 kgCO2/kgmethyl chloride, for hydrochlorination of methanol. These emissions are mainly due to the electricity required in the electrolyzer and could be reduced to −0.5 kgCO2/kgmethyl chloride (CO2 is absorbed) if the electricity source is fully renewable.es_ES
dc.description.sponsorship“Tecnologías, materiales y procesos para producción a pequeña escala de portadores de hidrógeno renovable (metano y amoniaco) para un aprovechamiento distribuido≫─Plan de Recuperación, Transformación y Resiliencia─Next Generation UE ProyH2Amo.es_ES
dc.format.mimetypeapplication/pdf
dc.language.isoenges_ES
dc.publisherAmerican Chemical Societyes_ES
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectCO2 utilizationes_ES
dc.subjectWaste brinees_ES
dc.subjectChlorine industryes_ES
dc.subjectElectrolysises_ES
dc.subjectMathematical optimizationes_ES
dc.subject.meshChemical Processes *
dc.titleEconomic and Environmental Comparison of Integrated Processes to Produce Chloromethanes from Brine Waste and CO2.es_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publishversionhttps://doi.org/10.1021/acssuschemeng.3c01627es_ES
dc.subject.unesco3303.11 Química Industriales_ES
dc.identifier.doi10.1021/acssuschemeng.3c01627
dc.relation.projectIDProyH2Amoes_ES
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses_ES
dc.identifier.essn2168-0485
dc.journal.titleACS Sustainable Chemistry & Engineeringes_ES
dc.volume.number11es_ES
dc.issue.number31es_ES
dc.page.initial11502es_ES
dc.page.final11515es_ES
dc.type.hasVersioninfo:eu-repo/semantics/submittedVersiones_ES
dc.subject.decsProcesos químicos *


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