<?xml version="1.0" encoding="UTF-8"?>
<collection>
<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:identifier>doi:10.1016/j.cej.2025.164562</dc:identifier><dc:language>eng</dc:language><dc:creator>González-Pizarro, R.</dc:creator><dc:creator>Lasobras, J.</dc:creator><dc:creator>Soler, J.</dc:creator><dc:creator>Herguido, J.</dc:creator><dc:creator>Menéndez, M.</dc:creator><dc:title>Proof of concept for a sorption-enhanced reactor with continuous sorbent feeding (CSF): application to green methanol production</dc:title><dc:identifier>ART-2025-144243</dc:identifier><dc:description>A new reactor for process intensification using sorption enhanced reaction is described. The novelty compared with most experimental work is that a continuous sorbent feeding (CSF) provides a steady state operation. The sorbent increases the reaction rate of a reversible reaction. The reactor is based on the phenomena of segregation of solids in fluidized bed reactors by using a catalyst and a sorbent. Under certain conditions of density and particle size, the two solids segregate and the sorbent may be removed from the bed with only a small content of catalyst. The system has been experimentally tested in the hydrogenation of CO2 to methanol, using a zeolite as sorbent. A significant increase in CO2 conversion was achieved compared with the same reactor without sorbent.</dc:description><dc:date>2025</dc:date><dc:source>http://zaguan.unizar.es/record/161046</dc:source><dc:doi>10.1016/j.cej.2025.164562</dc:doi><dc:identifier>http://zaguan.unizar.es/record/161046</dc:identifier><dc:identifier>oai:zaguan.unizar.es:161046</dc:identifier><dc:relation>info:eu-repo/grantAgreement/ES/AEI/PID2022-139819OB-I00</dc:relation><dc:relation>info:eu-repo/grantAgreement/ES/MICINN/PDC2022-133066-I00</dc:relation><dc:identifier.citation>Chemical Engineering Journal 517 (2025), 164562 [8 pp.]</dc:identifier.citation><dc:rights>by</dc:rights><dc:rights>https://creativecommons.org/licenses/by/4.0/deed.es</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

</collection>