Dynamic Models Of Industrial Hdt Reactor

dc.creatorVasco De Toledo E.C.
dc.creatorDe Morais E.R.
dc.creatorMariano A.P.
dc.creatorMelo D.N.C.
dc.creatorConcha V.O.C.
dc.creatorMeyer J.F.C.A.
dc.creatorFilho R.M.
dc.date2006
dc.date2015-06-30T18:05:01Z
dc.date2015-11-26T14:22:33Z
dc.date2015-06-30T18:05:01Z
dc.date2015-11-26T14:22:33Z
dc.date.accessioned2018-03-28T21:24:28Z
dc.date.available2018-03-28T21:24:28Z
dc.identifier8086059456; 9788086059457
dc.identifierChisa 2006 - 17th International Congress Of Chemical And Process Engineering. , v. , n. , p. - , 2006.
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dc.identifierhttp://www.scopus.com/inward/record.url?eid=2-s2.0-34748876592&partnerID=40&md5=ce551afd029c9442e6b9104bf4e8cb99
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/103006
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/103006
dc.identifier2-s2.0-34748876592
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1244865
dc.descriptionThe hydrodesulfurization (HDS), hydrodenitrogenation (HDN), hydrodeoxygenation, hydrocraking and saturative hydrogenation of middle distillates were studied in this work. An adiabatic diesel hydrotreating packed trickle bed reactor was simulated numerically in order to check up the dynamic behaviour of this specific reaction system. The model consists of mass and heat balance equations, and variations in the physical properties as well as in the heat and mass transfer coefficients. The proposed model was able to predict the main characteristics of the dynamic behaviour of the reactor. Therefore, it is possible to use the model for a specific application, especially to design, control and optimization on-line.
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dc.languageen
dc.publisher
dc.relationCHISA 2006 - 17th International Congress of Chemical and Process Engineering
dc.rightsfechado
dc.sourceScopus
dc.titleDynamic Models Of Industrial Hdt Reactor
dc.typeActas de congresos


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