{"data":{"id":"10.6084/m9.figshare.7185908","type":"dois","attributes":{"doi":"10.6084/m9.figshare.7185908","prefix":"10.6084","suffix":"m9.figshare.7185908","identifiers":[],"alternateIdentifiers":[],"creators":[{"name":"Moura, Rafael B.","nameType":"Personal","givenName":"Rafael B.","familyName":"Moura","affiliation":[],"nameIdentifiers":[]},{"name":"Damasceno, Leonardo H. S.","nameType":"Personal","givenName":"Leonardo H. S.","familyName":"Damasceno","affiliation":[],"nameIdentifiers":[]},{"name":"Damianovic, Márcia H.R.Z.","nameType":"Personal","givenName":"Márcia H.R.Z.","familyName":"Damianovic","affiliation":[],"nameIdentifiers":[]},{"name":"Zaiat, Marcelo","nameType":"Personal","givenName":"Marcelo","familyName":"Zaiat","affiliation":[],"nameIdentifiers":[]},{"name":"Foresti, Eugenio","nameType":"Personal","givenName":"Eugenio","familyName":"Foresti","affiliation":[],"nameIdentifiers":[]}],"titles":[{"title":"HYDRODYNAMIC CHARACTERISTICS OF A STRUCTURED BED REACTOR SUBJECTED TO RECIRCULATION AND INTERMITTENT AERATION (SBRRIA)"}],"publisher":"SciELO journals","container":{},"publicationYear":2018,"subjects":[{"subject":"90499 Chemical Engineering not elsewhere classified","subjectScheme":"FOR"},{"subject":"FOS: Chemical engineering","schemeUri":"http://www.oecd.org/science/inno/38235147.pdf","subjectScheme":"Fields of Science and Technology (FOS)"},{"subject":"FOS: Chemical engineering","subjectScheme":"Fields of Science and Technology (FOS)"}],"contributors":[],"dates":[{"date":"2018-10-10","dateType":"Created"},{"date":"2018-10-10","dateType":"Updated"},{"date":"2018","dateType":"Issued"}],"language":null,"types":{"ris":"DATA","bibtex":"misc","citeproc":"dataset","schemaOrg":"Dataset","resourceType":"Dataset","resourceTypeGeneral":"Dataset"},"relatedIdentifiers":[{"relationType":"IsSupplementTo","relatedIdentifier":"10.1590/0104-6632.20180352s20160516","relatedIdentifierType":"DOI"}],"relatedItems":[],"sizes":["1302935 Bytes"],"formats":[],"version":null,"rightsList":[{"rights":"Creative Commons Attribution 4.0 International","rightsUri":"https://creativecommons.org/licenses/by/4.0/legalcode","schemeUri":"https://spdx.org/licenses/","rightsIdentifier":"cc-by-4.0","rightsIdentifierScheme":"SPDX"}],"descriptions":[{"description":"ABSTRACT This work aimed at evaluating the effect of recirculation ratio on the degree of mixing in the flow of a structured bed reactor. Stimulus-response assays were carried out with hydraulic retention times of 6 h and 12 h, subjected to recirculation ratios of 0, 1, 2, 3, and 4. The assays were undertaken with dextran blue as a tracer and without aeration. The results fitted a compartment model, allowing the determination of the mixed-flow and plug-flow volumes inside the reactor. The model application showed that recirculation ratios between 1 and 3 do not increase the mixed-flow volume of the reactor. Higher mixed-flow volumes were obtained at recirculation rates higher than 4 for both 6 h and 12 h of hydraulic retention times. The results obtained in this research are important for future applications of this reactor configuration, promoting a mixed flow in the reactor with a minimum recirculation ratio.","descriptionType":"Abstract"}],"geoLocations":[],"fundingReferences":[],"xml":"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","url":"https://scielo.figshare.com/articles/HYDRODYNAMIC_CHARACTERISTICS_OF_A_STRUCTURED_BED_REACTOR_SUBJECTED_TO_RECIRCULATION_AND_INTERMITTENT_AERATION_SBRRIA_/7185908","contentUrl":null,"metadataVersion":2,"schemaVersion":"http://datacite.org/schema/kernel-4","source":"mds","isActive":true,"state":"findable","reason":null,"viewCount":0,"viewsOverTime":[],"downloadCount":0,"downloadsOverTime":[],"referenceCount":1,"citationCount":0,"citationsOverTime":[],"partCount":0,"partOfCount":0,"versionCount":0,"versionOfCount":0,"created":"2018-10-10T02:48:17.000Z","registered":"2018-10-10T02:49:21.000Z","published":"2018","updated":"2020-08-28T07:57:28.000Z"},"relationships":{"client":{"data":{"id":"figshare.ars","type":"clients"}},"provider":{"data":{"id":"otjm","type":"providers"}},"media":{"data":{"id":"10.6084/m9.figshare.7185908","type":"media"}},"references":{"data":[{"id":"10.1590/0104-6632.20180352s20160516","type":"dois"}]},"citations":{"data":[]},"parts":{"data":[]},"partOf":{"data":[]},"versions":{"data":[]},"versionOf":{"data":[]}}}}