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<dc:title>Evaluating the experimental CO2 stripping performance of a new generation multicapillary Taylor flow reactor</dc:title>
<dc:creator>Vargas Estrada, Laura Gabriela</dc:creator>
<dc:creator>Bordel Velasco, Sergio</dc:creator>
<dc:creator>Lebrero Fernández, Raquel</dc:creator>
<dc:creator>Muñoz Torre, Raúl</dc:creator>
<dcterms:abstract>Among all physicochemical technologies commercially available to upgrade biogas to biomethane, chemical&#xd;
scrubbing with carbonated solutions stand as an easy-to-scale technology. However, the regeneration of the&#xd;
solvent via air-assisted CO2 stripping is highly energy-intensive, representing >80 % of the total process costs.&#xd;
This study proposes the use of innovative Taylor flow reactors to enhance the liquid-gas mass transfer of CO2 and&#xd;
therefore lower the cost of regeneration of carbonated solutions. In this study, a 200-glass capillary Taylor flow&#xd;
reactor supporting unprecedented mass transfer coefficients (kLa) was tested for the first time for CO2 stripping&#xd;
from carbonated solutions. The Taylor flow reactor achieved kLa coefficients higher than 100 h-1 at an inorganic&#xd;
concentration (IC) of 1000 mgC L-1, and kLa > 400 h-1 at an optimal gas superficial velocity of 0.30 m s-1.&#xd;
Moreover, increasing IC concentrations to 2000 and 3000 mgC L-1 resulted in a kLa increase of 250 % and 65 %,&#xd;
respectively, whilst no significant increase was recorded at an initial IC concentration of 4000 mgC L-1. Indeed,&#xd;
multicapillary Taylor flow reactors demonstrated a superior and competitive performance during CO2 stripping&#xd;
from carbonated solutions, representing a promising technology for solvent regeneration during biogas&#xd;
upgrading at industrial scale.</dcterms:abstract>
<dcterms:dateAccepted>2025-11-26T11:38:58Z</dcterms:dateAccepted>
<dcterms:available>2025-11-26T11:38:58Z</dcterms:available>
<dcterms:created>2025-11-26T11:38:58Z</dcterms:created>
<dcterms:issued>2026</dcterms:issued>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>Chemical Engineering and Processing - Process Intensification, 2026, vol. 219, p. 110601</dc:identifier>
<dc:identifier>0255-2701</dc:identifier>
<dc:identifier>https://uvadoc.uva.es/handle/10324/80088</dc:identifier>
<dc:identifier>10.1016/j.cep.2025.110601</dc:identifier>
<dc:identifier>110601</dc:identifier>
<dc:identifier>Chemical Engineering and Processing - Process Intensification</dc:identifier>
<dc:identifier>219</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>https://www.sciencedirect.com/science/article/pii/S0255270125004477</dc:relation>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by-nc/4.0/</dc:rights>
<dc:rights>© 2025 The Author(s)</dc:rights>
<dc:rights>Atribución-NoComercial 4.0 Internacional</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
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