Issue |
E3S Web Conf.
Volume 13, 2017
4th Scientific and Technical Conference on Modern Technologies and Energy Systems, WTiUE 2016
|
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Article Number | 04002 | |
Number of page(s) | 9 | |
Section | Mathematical modeling in the energy and industrial processes | |
DOI | https://doi.org/10.1051/e3sconf/20171304002 | |
Published online | 10 February 2017 |
Numerical simulations of fluidization dynamics in a hot model of a CLC process
1 Czestochowa University of Technology, Faculty of Infrastructure and Environment, Institute of Advanced Energy Technologies, J.H. Dabrowskiego 73, 42-200 Czestochowa, Poland
2 Jan Dlugosz University in Czestochowa, Institute of Technology and Safety Systems, Armii Krajowej 13/15, 42-200 Czestochowa, Poland
3 AGH University of Science and Technology, Department of Thermal Machinery and Flow, Faculty of Energy and Fuels, Czarnowiejska 50B, I, 30-054 Cracow, Poland
* Corresponding author: azylka@is.pcz.pl
Chemical Looping Combustion (CLC) is one of the most promising alternatives for solid fuel combustion. CO2 concentration in the exhaust gas is high in CLC technology which enables high efficiency of CO2 capture from flue gas. The use of solid oxygen carriers is a characteristic feature of a CLC process. Oxygen carriers are mainly metal oxides which are characterized by high oxygen transfer capacity and high mechanical resistance.
Since the CLC technology is not sufficiently recognized due to its complexity the development of models with real conditions of the CLC equipment is of practical significance.
The paper presents numerical simulations of the dynamic fluidized bed for Chemical Looping Combustion using CeSFaMB software. The model was validated on the basis of the results obtained from experiments, which were carried out on the Fluidized-Bed Chemical-Looping-Combustion of Solid-Fuels (FB-CLC-SF) unit. The studies were conducted in air atmosphere at temperature of 850°C. The validation of the 1.5D model showed that the maximum relative error between experiment and simulations results does not exceed 12%.
© The Authors, published by EDP Sciences, 2017
This is an Open Access article distributed under the terms of the Creative Commons Attribution License 4.0, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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