Resumen: A simulation of the catalytic CO2 methanation reaction was carried out, evaluating the effect of reactants distributed feeding throughout the bed. The main operational parameters were studied in a multiple-inlet reactor to test their effect on conversions and, most importantly, on selectivities towards both CO and CH4 as reaction products. The analyzed parameters were, firstly, the number of feeding points (N) and the dosage degree of reactants, followed by temperature (T), partial pressures of reactants (H2:CO2 ratios), and the composition of a sweetened biogas as feeding stream (CH4:CO2 ratios). It is confirmed that a distribution of biogas through several side inlets improves selectivities to the desired CH4 product, over other feeding configurations. The effect of distributing reactants becomes intensified when the number of lateral feedings increases. This observation supports the experimental trends already proven in previous works. Regarding main operation parameters such as temperature and H2:CO2 molar ratio, the analysis confirmed that their influence on selectivities acts just as predicted at low conversions. However, when these conversions become higher the space velocity (WHSV) is the most important factor for selectivities. Finally, no significant changes in reaction performance were obtained when modifying the biogas CH4:CO2 ratio in the broad range of methane concentrations from 55 v% to 70 v%. Idioma: Inglés DOI: 10.1016/j.jcou.2025.103038 Año: 2025 Publicado en: Journal of CO2 Utilization 93 (2025), 103038 [10 pp.] ISSN: 2212-9820 Financiación: info:eu-repo/grantAgreement/ES/AEI/PID2022-136947OB-I00 Financiación: info:eu-repo/grantAgreement/ES/DGA/T43-23R Financiación: info:eu-repo/grantAgreement/ES/MICINN/PRE2020-095679 Tipo y forma: Article (Published version) Área (Departamento): Área Ingeniería Química (Dpto. Ing.Quím.Tecnol.Med.Amb.) Área (Departamento): Proy. investigación HKA (Dpto. Ing.Quím.Tecnol.Med.Amb.)
Exportado de SIDERAL (2025-10-17-14:28:01)