dc.creatorCarbonell M.M.
dc.creatorGuirardello R.
dc.date1997
dc.date2015-06-30T14:47:56Z
dc.date2015-11-26T15:26:46Z
dc.date2015-06-30T14:47:56Z
dc.date2015-11-26T15:26:46Z
dc.date.accessioned2018-03-28T22:35:27Z
dc.date.available2018-03-28T22:35:27Z
dc.identifier
dc.identifierChemical Engineering Science. Elsevier Science Ltd, Oxford, United Kingdom, v. 52, n. 21-22, p. 4179 - 4185, 1997.
dc.identifier92509
dc.identifier
dc.identifierhttp://www.scopus.com/inward/record.url?eid=2-s2.0-0031278335&partnerID=40&md5=c5b76184b9e6fcdfcdfec8f1347fa7f2
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/100035
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/100035
dc.identifier2-s2.0-0031278335
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1261186
dc.descriptionThis work uses a computational fluid dynamics approach for the simulation of a slurry bubble column reactor, applied in the hydroconversion of heavy oils under severe temperature and pressure operating conditions. Simulations are carried out in two steps: first, the fluid dynamics is determined by the calculation of the pressure drop in the bed and the radial distribution of gas and slurry for the holdup, effective viscosity (dispersion) and velocity. Then a thermal cracking reaction is simulated and the oil conversion to lighter fractions such as gasoil, diesel, naphtha and gases is obtained. Results show the recirculation pattern in the reactor which leads to a high degree of backmixing in the slurry phase. Temperature and liquid residence time are found to have a great influence in the oil cracking conversion.This work uses a computational fluid dynamics approach for the simulation of a slurry bubble column reactor, applied in the hydroconversion of heavy oils under severe temperature and pressure operating conditions. Simulations are carried out in two steps: first, the fluid dynamics is determined by the calculation of the pressure drop in the bed and the radial distribution of gas and slurry for the holdup, effective viscosity (dispersion) and velocity. Then a thermal cracking reaction is simulated and the oil conversion to lighter fractions such as gasoil, diesel, naphtha and gases is obtained. Results show the recirculation pattern in the reactor which leads to a high degree of backmixing in the slurry phase. Temperature and liquid residence time are found to have a great influence in the oil cracking conversion.
dc.description52
dc.description21-22
dc.description4179
dc.description4185
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dc.languageen
dc.publisherElsevier Science Ltd, Oxford, United Kingdom
dc.relationChemical Engineering Science
dc.rightsfechado
dc.sourceScopus
dc.titleModelling Of A Slurry Bubble Column Reactor Applied To The Hydroconversion Of Heavy Oils
dc.typeActas de congresos


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