O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a
| Autor(a) principal: | |
|---|---|
| Data de Publicação: | 2015 |
| Outros Autores: | , |
| Tipo de documento: | Artigo |
| Idioma: | eng |
| Título da fonte: | Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) |
| Texto Completo: | https://hdl.handle.net/1822/31551 |
Resumo: | In the present work the superficial gas velocities ( u G ) and the oscillatory conditions (frequency and amplitude) effects on the gas–liquid mass transfer process in a novel oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) are experimentally evaluated. The liquid-side mass transfer coefficient, k L , and the specific interfacial area, a, are studied individually. The specific interfacial area is obtained using the new automatic image analysis technique developed by Ferreira et al. (2012). The experimental results of volumetric liquid side mass transfer coefficient ( k L a ), Sauter mean diameter ( d 32 ) and gas holdup ( ε G ), and the calculated values of a and k L , are correlated with the superficial gas velocity and the power density ( P / V ), in order to be used in scale-up processes and in comparisons with the literature. The results show that k L a increases with both superficial gas velocity and oscillatory conditions, the last ones having the highest impact on the mass transfer process. The increase in the oscillation motion (frequency and amplitude) results in bubble size reduction (from ∼7 mm, without oscillation, to ∼1 mm, with oscillation), in bubble average residence time increase and, consequently, in a increase. A k L increase with d 32 decrease is observed, showing the importance of hydrodynamic phenomena on k L , specially, when very low bubbles sizes are presented in oscillatory flow reactors. |
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O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and aOscillatory flow reactorMultiphase reactorsMass transferLiquid-side mass transfer coefficientSpecific interfacial areaScience & TechnologyIn the present work the superficial gas velocities ( u G ) and the oscillatory conditions (frequency and amplitude) effects on the gas–liquid mass transfer process in a novel oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) are experimentally evaluated. The liquid-side mass transfer coefficient, k L , and the specific interfacial area, a, are studied individually. The specific interfacial area is obtained using the new automatic image analysis technique developed by Ferreira et al. (2012). The experimental results of volumetric liquid side mass transfer coefficient ( k L a ), Sauter mean diameter ( d 32 ) and gas holdup ( ε G ), and the calculated values of a and k L , are correlated with the superficial gas velocity and the power density ( P / V ), in order to be used in scale-up processes and in comparisons with the literature. The results show that k L a increases with both superficial gas velocity and oscillatory conditions, the last ones having the highest impact on the mass transfer process. The increase in the oscillation motion (frequency and amplitude) results in bubble size reduction (from ∼7 mm, without oscillation, to ∼1 mm, with oscillation), in bubble average residence time increase and, consequently, in a increase. A k L increase with d 32 decrease is observed, showing the importance of hydrodynamic phenomena on k L , specially, when very low bubbles sizes are presented in oscillatory flow reactors.This work was supported by Fundacao para a Ciencia e Tecnologia under program contract number SFRH/BPD/45637/2008.Elsevier B.V.Universidade do MinhoFerreira, AntónioTeixeira, J. A.Rocha, F. A.20152015-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttps://hdl.handle.net/1822/31551engFerreira, António; Teixeira, José A.; Rocha, F., O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions. Individual characterization of kl and a. Chemical Engineering Journal, 262, 499-508, 20151385-89471385-894710.1016/j.cej.2014.09.125info:eu-repo/semantics/openAccessreponame:Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)instname:FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiainstacron:RCAAP2025-04-12T04:33:17Zoai:repositorium.sdum.uminho.pt:1822/31551Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireinfo@rcaap.ptopendoar:https://opendoar.ac.uk/repository/71602025-05-28T15:23:25.705869Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) - FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiafalse |
| dc.title.none.fl_str_mv |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| title |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| spellingShingle |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a Ferreira, António Oscillatory flow reactor Multiphase reactors Mass transfer Liquid-side mass transfer coefficient Specific interfacial area Science & Technology |
| title_short |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| title_full |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| title_fullStr |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| title_full_unstemmed |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| title_sort |
O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions : individual characterization of kL and a |
| author |
Ferreira, António |
| author_facet |
Ferreira, António Teixeira, J. A. Rocha, F. A. |
| author_role |
author |
| author2 |
Teixeira, J. A. Rocha, F. A. |
| author2_role |
author author |
| dc.contributor.none.fl_str_mv |
Universidade do Minho |
| dc.contributor.author.fl_str_mv |
Ferreira, António Teixeira, J. A. Rocha, F. A. |
| dc.subject.por.fl_str_mv |
Oscillatory flow reactor Multiphase reactors Mass transfer Liquid-side mass transfer coefficient Specific interfacial area Science & Technology |
| topic |
Oscillatory flow reactor Multiphase reactors Mass transfer Liquid-side mass transfer coefficient Specific interfacial area Science & Technology |
| description |
In the present work the superficial gas velocities ( u G ) and the oscillatory conditions (frequency and amplitude) effects on the gas–liquid mass transfer process in a novel oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) are experimentally evaluated. The liquid-side mass transfer coefficient, k L , and the specific interfacial area, a, are studied individually. The specific interfacial area is obtained using the new automatic image analysis technique developed by Ferreira et al. (2012). The experimental results of volumetric liquid side mass transfer coefficient ( k L a ), Sauter mean diameter ( d 32 ) and gas holdup ( ε G ), and the calculated values of a and k L , are correlated with the superficial gas velocity and the power density ( P / V ), in order to be used in scale-up processes and in comparisons with the literature. The results show that k L a increases with both superficial gas velocity and oscillatory conditions, the last ones having the highest impact on the mass transfer process. The increase in the oscillation motion (frequency and amplitude) results in bubble size reduction (from ∼7 mm, without oscillation, to ∼1 mm, with oscillation), in bubble average residence time increase and, consequently, in a increase. A k L increase with d 32 decrease is observed, showing the importance of hydrodynamic phenomena on k L , specially, when very low bubbles sizes are presented in oscillatory flow reactors. |
| publishDate |
2015 |
| dc.date.none.fl_str_mv |
2015 2015-01-01T00:00:00Z |
| dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
| dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
| format |
article |
| status_str |
publishedVersion |
| dc.identifier.uri.fl_str_mv |
https://hdl.handle.net/1822/31551 |
| url |
https://hdl.handle.net/1822/31551 |
| dc.language.iso.fl_str_mv |
eng |
| language |
eng |
| dc.relation.none.fl_str_mv |
Ferreira, António; Teixeira, José A.; Rocha, F., O2 mass transfer in an oscillatory flow reactor provided with smooth periodic constrictions. Individual characterization of kl and a. Chemical Engineering Journal, 262, 499-508, 2015 1385-8947 1385-8947 10.1016/j.cej.2014.09.125 |
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info:eu-repo/semantics/openAccess |
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openAccess |
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application/pdf |
| dc.publisher.none.fl_str_mv |
Elsevier B.V. |
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Elsevier B.V. |
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Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) - FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologia |
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