Interfacial area and mass transfer in carbon dioxide absorption in TEA aqueous solutions in a bubble column reactor |
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Authors: | M. Dolores La Rubia,Alicia Garcí a-Abuí n,Diego Gó mez-Dí az,José M. Navaza |
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Affiliation: | 1. Department of Chemical, Environmental and Materials Engineering, EPS, University of Jaén, Paraje Las Lagunillas s/n, E-23071 Jaén, Spain;2. Department of Chemical Engineering, ETSE, University of Santiago de Compostela, Rúa Lope Gómez de Marzoa s/n, E-15706 Santiago de Compostela, Spain |
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Abstract: | The hydrodynamic behaviour and mass transfer of carbon dioxide removal process by aqueous solutions of triethanolamine (TEA) are analysed. The experiments were made in a bubble column reactor (BCR) as gas–liquid contactor. The interfacial area and mass transfer coefficient were calculated by using a photographic method based on the bubble diameter determination. The influence of operation conditions, liquid phase nature and chemical reaction on the mass transfer coefficient and gas–liquid interfacial area has been also analysed. |
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Keywords: | Absorption Carbon dioxide Amine Bubble column |
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