Utilize este identificador para referenciar este registo: https://hdl.handle.net/1822/83832

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Campo DCValorIdioma
dc.contributor.authorAlmeida, F.por
dc.contributor.authorRocha, F.por
dc.contributor.authorTeixeira, J. A.por
dc.contributor.authorFerreira, A.por
dc.date.accessioned2023-04-06T10:55:38Z-
dc.date.available2023-04-06T10:55:38Z-
dc.date.issued2023-05-
dc.identifier.citationAlmeida, F.; Rocha, F.; Teixeira, José A.; Ferreira, A., Hydrodynamics and gas-liquid mass transfer in an oscillatory flow reactor: influence of liquid properties. Chemical Engineering Research & Design, 193, 179-197, 2023por
dc.identifier.issn0263-8762por
dc.identifier.urihttps://hdl.handle.net/1822/83832-
dc.descriptionAvailable online 20 March 2023por
dc.description.abstractLiquid properties, such as, surface tension and viscosity are important parameters as they control gas-liquid mass transfer in bioprocesses. An oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) was considered to evaluate its potential for mass transfer performance in non-pure gas-liquid systems. The effect of surface tension and viscosity on the volumetric (kLa) and liquid-side mass transfer coefficients (kL), interfacial area, (a), gas holdup (G) and bubbles dynamics were investigated under different operational conditions (oscillation amplitude (x0) and frequency (f) and superficial gas velocity (ug)). Two liquid phases, ethanol and sucrose aqueous solutions covering a range of surface tension and viscosity values were used. For the bubble size distribution (BSD) measurements an image analysis technique was used. A Design of Experiment (DoE) methodology was implemented in this work to establish the relation of x0, f, ug, surface tension and viscosity with kLa. According to the results, changes in the liquid properties and operational conditions showed marked effects on bubbles size and mass transfer. However, surface tension and viscosity had no significant influence on G, contrary to the reported for common contactors, where G increased in the presence of ethanol and decreased at moderate/high viscosities. Moreover, it was found that increasing the oscillatory movement notably improved kL, and kLa (2 to 6-fold), either in ethanol or sucrose solutions, compared to common reactors, even with moderate power consumption (~105 W m-3). This improvement resulted from the bubbles breakage, which originates bubbles with small and approximately the same size (homogeneous regime) enhancing a, instead, lower oscillations resulted in large bubbles (heterogeneous regime). The results demonstrate that the OFR-SPC can ensure outstanding mass transfer rates, with potential and feasibility for use in gas-liquid bioprocesses, where mass transfer and liquid properties are important.por
dc.description.sponsorshipThis work was financially supported by: I) Project PTDC/QEQ-PRS/3787/2014 -POCI-01–0145-FEDER-016816 - funded by the European Regional Development Fund (ERDF) through COMPETE2020 -Programa Operacional Competitividade e Internacionalização (POCI) and by national funds through Fundaç ão para a Ciência e a Tecnologia.I.P. (FCT) - Project 9471 - Reforçar a Investigaç ão,o Desenvolvimento Tecnológico e a Inovaç ão; II) IF exploratory Project [IF/01087/2014] funded by FCT; III) LA/P/0045/2020 (ALiCE), UIDB/00511/2020 and UIDP/00511/2020 (LEPABE), funded by national funds through FCT/MCTES (PIDDAC); IV) the FCT under the scope of the strategic funding of UIDB/04469/2020 unit, and by LABBELS – Associate Laboratory in Biotechnology, Bioengineering and Microelectromechnaical Systems, LA/P/0029/2020. A. Ferreira is an Investigador FCT. F. Almeida would wish to thank to FCT for PhD scholarship 2020.05246. BD.por
dc.language.isoengpor
dc.publisherElsevier 1por
dc.relationinfo:eu-repo/grantAgreement/FCT/9471 - RIDTI/PTDC%2FQEQ-PRS%2F3787%2F2014/PTpor
dc.relationinfo:eu-repo/grantAgreement/FCT/Investigador FCT/IF%2F01087%2F2014%2FCP1249%2FCT0001/PTpor
dc.relation0por
dc.relationinfo:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F00511%2F2020/PTpor
dc.relationinfo:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDP%2F00511%2F2020/PTpor
dc.rightsopenAccesspor
dc.subjectOscillatory flow reactorpor
dc.subjectGas-liquid mass transferpor
dc.subjectGas holduppor
dc.subjectSauter mean diameterpor
dc.subjectDesign of experiments (DoE)por
dc.subjectMultiphase reactorspor
dc.titleHydrodynamics and gas-liquid mass transfer in an oscillatory flow reactor: influence of liquid propertiespor
dc.typearticle-
dc.peerreviewedyespor
dc.relation.publisherversionhttp://www.journals.elsevier.com/chemical-engineering-research-and-design/por
dc.commentsCEB56124por
oaire.citationStartPage179por
oaire.citationEndPage197por
oaire.citationConferencePlaceUnited Kingdom-
oaire.citationVolume193por
dc.date.updated2023-04-03T14:43:09Z-
dc.identifier.doi10.1016/j.cherd.2023.03.030por
dc.description.publicationversioninfo:eu-repo/semantics/publishedVersion-
dc.subject.wosScience & Technologypor
sdum.journalChemical Engineering Research & Designpor
oaire.versionP-
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