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               <dc:title>Design of a Multi-Tubular Catalytic Reactor Assisted by CFD Based on Free-Convection Heat-Management for Decentralised Synthetic Methane Production</dc:title>
               <dc:creator>Alarcón Avellán, Andreina</dc:creator>
               <dc:creator>Busqué, Raquel</dc:creator>
               <dc:creator>Andreu Arbella, Teresa</dc:creator>
               <dc:creator>Guilera Sala, Jordi</dc:creator>
               <dc:subject>Reactors químics</dc:subject>
               <dc:subject>Diòxid de carboni</dc:subject>
               <dc:subject>Metà</dc:subject>
               <dc:subject>Chemical reactors</dc:subject>
               <dc:subject>Carbon dioxide</dc:subject>
               <dc:subject>Methane</dc:subject>
               <dc:description>A simple reactor design for the conversion of CO2 methanation into synthetic methane based on free convection is an interesting option for small-scale, decentralised locations. In this work, we present a heat-management design of a multi-tubular reactor assisted by CFD (Ansys Fluent®) as an interesting tool for scaling-up laboratory reactor designs. The simulation results pointed out that the scale-up of an individual reactive channel (d = 1/4′, H = 300 mm) through a hexagonal-shaped distribution of 23 reactive channels separated by 40 mm allows to obtain a suitable decreasing temperature profile (T = 487-230 °C) for the reaction using natural convection cooling. The resulting heat-management configuration was composed of three zones: (i) preheating of the reactants up to 230 °C, followed by (ii) a free-convection zone (1 m/s air flow) in the first reactor section (0-25 mm) to limit overheating and, thus, catalyst deactivation, followed by (iii) an isolation zone in the main reactor section (25-300 mm) to guarantee a proper reactor temperature and favourable kinetics. The evaluation of the geometry, reactive channel separation, and a simple heat-management strategy by CFD indicated that the implementation of an intensive reactor cooling system could be omitted with natural air circulation.</dc:description>
               <dc:date>2023-03-24T14:12:36Z</dc:date>
               <dc:date>2023-03-24T14:12:36Z</dc:date>
               <dc:date>2022-09-01</dc:date>
               <dc:date>2023-03-24T14:12:36Z</dc:date>
               <dc:type>info:eu-repo/semantics/article</dc:type>
               <dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
               <dc:relation>Reproducció del document publicat a: https://doi.org/10.3390/catal12091053</dc:relation>
               <dc:relation>Catalysts, 2022, vol. 12, num. 9, p. 1-19</dc:relation>
               <dc:relation>https://doi.org/10.3390/catal12091053</dc:relation>
               <dc:rights>cc-by (c) Alarcón Avellán, Andreina et al., 2022</dc:rights>
               <dc:rights>https://creativecommons.org/licenses/by/4.0/</dc:rights>
               <dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
               <dc:publisher>MDPI</dc:publisher>
               <dc:source>Articles publicats en revistes (Ciència dels Materials i Química Física)</dc:source>
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