Modeling and simulation of particles coating in fluidized bed
Modeling and Simulation of Nanoparticle production by Flame Spray Pyrolysis Using ...
Lattice Boltzmann simulation of hydrodynamics inside fixed-bed bioreactor for vina...
![]() | |
Author(s): |
Flavio Cesar Cunha Galeazzo
Total Authors: 1
|
Document type: | Master's Dissertation |
Press: | Campinas, SP. |
Institution: | Universidade Estadual de Campinas (UNICAMP). Faculdade de Engenharia Quimica |
Defense date: | 2005-10-25 |
Examining board members: |
José Roberto Nunhez;
Andre Gonçalves Antunha;
Efraim Cekinski
|
Advisor: | José Roberto Nunhez |
Abstract | |
The work analysed the impact of operating conditions and geometric changes in the thermal performance of a esterification industrial reactor of the company M&G. The analyses used a numerical model created with the aid of the software FLUENT. The simplifying hypothesis of considering only one liquid phase instead of the real system three phases was capable of showing the main characteristics of the flow and the heat transfer inside the reactor, like stagnation zones and impellers influence zones, and the heat transfer from the axial coil. The results lead to the conclusion that the agitation system have only a secundary role in the reactor thermal performance, while the role of the flow separation discs is dominant (AU) |