Please use this identifier to cite or link to this item: http://ir.futminna.edu.ng:8080/jspui/handle/123456789/978
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dc.contributor.authorAdeniyi, O.D.-
dc.contributor.authorAbdulkareem, A.S.-
dc.contributor.authorOdigure, J.O.-
dc.contributor.authorAweh, E.A.-
dc.contributor.authorNwokoro, U.T.-
dc.date.accessioned2021-06-03T11:27:19Z-
dc.date.available2021-06-03T11:27:19Z-
dc.date.issued2003-
dc.identifier.issn1513-0886-
dc.identifier.urihttp://repository.futminna.edu.ng:8080/jspui/handle/123456789/978-
dc.descriptionwww.journal.au.eduen_US
dc.description.abstractThis paper proposes a mathematical model for the operation of a non- ideal plug flow reactor in a saponification pilot plant of a typical process industry in Lagos, Nigeria. The residence time distribution (RTD) analysis technique involving tracer experiments was used. The model also gives a prediction of the number of ideal continuous stirred tank reactors (CSTR) that could represent the non-ideal plug flow reactor (PFR) in question. Simulated results reveals that 8.18 number of ideal stirred tanks in series would represent the non-ideal plug flow reactor under study.en_US
dc.language.isoenen_US
dc.publisherAssumption Univ. J. of Tech. (AUJT), Bangkok, Thailanden_US
dc.relation.ispartofseriesVol.7, No. 2 pp. 65-74;Vol.7, No. 2 pp. 65-74-
dc.subjectmodel, simulation, PFR, RTD, CSTR, NaOH, C17H35COOHen_US
dc.titleMathematical Modeling and simulation of a Non-Ideal Plug Flow Reactor in a Saponification Pilot Planten_US
dc.typeArticleen_US
Appears in Collections:Chemical Engineering

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