期刊
CHEMICAL ENGINEERING JOURNAL
卷 178, 期 -, 页码 129-137出版社
ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2011.10.026
关键词
Oxy-fuel; Fluidized bed; Fluid-dynamics; CO2 capture
资金
- Spanish Ministry of Science and Innovation (MICINN, Ministerio de Ciencia e Innovacion) [ENE-2009-08246]
- Fundacion CIUDEN
This paper addresses the mathematical development and the experimental validation of a semi-empirical model designed to characterize the fluid-dynamic response of a fluidized bed reactor under oxy-fuel operation. The objective is to survey the main differences between a conventional air operation and a novel O-2/CO2 operation, as for the interactions of solid-phase and gas-phase. The model provides all the relevant variables describing the fluid-dynamics, and it is conceived to simulate the performance of a lab-scale facility. Data gathered from the cold- and hot-operation of a 90 kW(th), oxy-fired fluidized bed are used for validation purposes. Bed porosity, minimum fluidization velocity and bubbles' size are detected to change under oxy-firing conditions. Once validated, the tool will he used to predict the performance under new fluidizing atmospheres and will be integrated within an entire model coupling fluid-dynamics, combustion and heat transfer phenomena. (C) 2011 Elsevier B.V. All rights reserved.
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