This work presents the numerical results of the computational fluid dynamics of a semi batch reactor used for hydroconversion of heavy oil. The reactor is a multicomponent system, and it is modeled as a pseudo two phase system (gas+slurry). The equations used are the continuity equations, the momentum equation (Navier-Stokes), and the k-ε for turbulence. The numerical method used to solve the mathematical method was the finite volume, where the problem was divided in two domains, in order to account for the moving part of the impeller. The numerical results indicated convergence of the procedure for the velocity profiles. © 2009 American Institute of Physics.1148 2281284Yamada, T.S., Guirardello, R., Kinetics and fluid dynamics for oil resi...
This study used a computational fluid dynamics simulation of an inert-particle spouted-bed reactor, ...
Research Doctorate - Doctor of Philosophy (PhD)This thesis describes a study in which the aim was to...
This work is presented as part of a preliminary study to model transesterification of Waste Cooking...
This paper deals with the modelling of a hydroconversion reactor, operating in a slurry bubble colum...
This work uses a computational fluid dynamics approach for the simulation of a slurry bubble column ...
This work presents a model to predict the behavior of velocity, gas holdup and local concentration f...
Orientador: Milton MoriTese (doutorado) - Universidade Estadual de Campinas, Faculdade de Engenharia...
A four-lump computational fluid dynamic (CFD) model was proposed for the investigation of vacuum ga...
This work presents the study of the flow distribution in a crude oil storage tank of 36.5 m of diame...
Because of the continuous increase in the amount of plastic waste, catalytic cracking is an interest...
This work presents a model to describe the behavior of the concentration of constituents of heavy fr...
In this research, computational fluid dynamics was applied to model a laboratory reactor for the deg...
In this paper, the numerical modeling of alkali-catalyzed waste cooking oil (WCO) transesterificatio...
Petroleum is a highly valued natural resource where the used are never ending and the demand will al...
The research aims to scale up a small-scale stirred batch reactor to a large-scale stirred batch rea...
This study used a computational fluid dynamics simulation of an inert-particle spouted-bed reactor, ...
Research Doctorate - Doctor of Philosophy (PhD)This thesis describes a study in which the aim was to...
This work is presented as part of a preliminary study to model transesterification of Waste Cooking...
This paper deals with the modelling of a hydroconversion reactor, operating in a slurry bubble colum...
This work uses a computational fluid dynamics approach for the simulation of a slurry bubble column ...
This work presents a model to predict the behavior of velocity, gas holdup and local concentration f...
Orientador: Milton MoriTese (doutorado) - Universidade Estadual de Campinas, Faculdade de Engenharia...
A four-lump computational fluid dynamic (CFD) model was proposed for the investigation of vacuum ga...
This work presents the study of the flow distribution in a crude oil storage tank of 36.5 m of diame...
Because of the continuous increase in the amount of plastic waste, catalytic cracking is an interest...
This work presents a model to describe the behavior of the concentration of constituents of heavy fr...
In this research, computational fluid dynamics was applied to model a laboratory reactor for the deg...
In this paper, the numerical modeling of alkali-catalyzed waste cooking oil (WCO) transesterificatio...
Petroleum is a highly valued natural resource where the used are never ending and the demand will al...
The research aims to scale up a small-scale stirred batch reactor to a large-scale stirred batch rea...
This study used a computational fluid dynamics simulation of an inert-particle spouted-bed reactor, ...
Research Doctorate - Doctor of Philosophy (PhD)This thesis describes a study in which the aim was to...
This work is presented as part of a preliminary study to model transesterification of Waste Cooking...