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A study of circulating fluidised bed combustion | |
Author | Das, Asit |
Call Number | AIT Thesis no. ET-89-02 |
Subject(s) | Fluidized-bed combustion |
Note | A thesis submitted in partial fulfillment of the requirements for the degree of Master of Engineering |
Publisher | Asian Institute of Technology |
Abstract | Biomass energy resource, in the developing countries, often contributes 50-90% of national energy demands and could meet more diverse energy needs through combustion in generating power and other heating requirements. Circulating Fluidised Bed (CFB) is an attractive technique of combustion which proved its special ability to burn a wide variety of solid biomass fuels. In the present work, a mathematical model for the steady state combustion of char in a CFB has been developed taking into account bed hydrodynamic conditions, chemical reaction rates, combustion mechanism and conservation of mass. The model is an improvement over the much simplified combustion model developed by BASU, SETT and GBORDZOE (1987). The present model, apart from a few other improvements, includes a fairly recent and an important aspect of solid backmixing i.e. solid flow down the combustor wall in a film as reported by BOLTON and DAVIDSON (1988). Variation of bed density along the height of the combustor, as a consequence to above phenomenon, has also been considered. The mode l has been used to predict oxygen and carbon concentrations along the height of the combustor. Since the model allows to consider a particle size distribution for the feed, it predicts fuel particle size distribution at the exit of the combustor. A CFB combustion system has been developed for which a successful startup procedure has been reported. Results from combustion tests of charcoal have been compared with model predictions. Experimental results showed qualitative agreement with the theory. Combustion test has been carried out with saw dust in order to make preliminary observations about capability of the CFB combustor to burn a fuel with characteristic high volatile content. The result shows somewhat poor efficiency (87.8%) at a low excess air level of 11%. |
Year | 1989 |
Type | Thesis |
School | School of Environment, Resources, and Development (SERD) |
Department | Department of Energy and Climate Change (Former title: Department of Energy, Environment, and Climate Change (DEECC)) |
Academic Program/FoS | Energy Technology (ET) |
Chairperson(s) | Bhattacharya, Sribas C.; |
Examination Committee(s) | Mora, Jean-Claude;Prida Wibulswas; |
Scholarship Donor(s) | The Royal Danish Government (DANIDA); |
Degree | Thesis (M.Eng.) - Asian Institute of Technology, 1989 |