THESIS
2014
xiv, 118 pages : illustrations (some color) ; 30 cm
Abstract
Solid waste treatment has drawn global attention in recent years. Incineration, as a
traditional solid waste treatment process, is an effective way to reduce the volume of solid
waste by 90%. However, greenhouse gases and toxic gases are produced during the
combustion process. Gasification, as a different thermochemical process, not only achieves
the purpose of a combustion process, but also has its own unique advantages. Gasification
means incomplete combustion and it results in the production of syngases. By controlling the
gasification agents (O
2, CO
2, air or stream), the concentration of different syngases can be
controlled. The gasification process is influenced by a number of parameters which include
temperature, concentration, flow rate and reaction surface area. In this...[
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Solid waste treatment has drawn global attention in recent years. Incineration, as a
traditional solid waste treatment process, is an effective way to reduce the volume of solid
waste by 90%. However, greenhouse gases and toxic gases are produced during the
combustion process. Gasification, as a different thermochemical process, not only achieves
the purpose of a combustion process, but also has its own unique advantages. Gasification
means incomplete combustion and it results in the production of syngases. By controlling the
gasification agents (O
2, CO
2, air or stream), the concentration of different syngases can be
controlled. The gasification process is influenced by a number of parameters which include
temperature, concentration, flow rate and reaction surface area. In this study, some existing
fluid-solid reaction models are reviewed. The Arrhenius equation is applied in most of the
reaction models in which the temperature and gas concentration are usually considered. For
solid waste gasification, another parameter, particle size, has a significant effect on
gasification rate as most of the solid wastes are not in powder form. In this research, the
effects of particle size are investigated by experiment, calculation and simulation.
In this study, the effects of different parameters are analyzed. The reaction rate and syngas
generation during gasification at different parameters are found by experiment. The effect of
concentration of gasification agents and the effect of particle size are investigated. Based on
the experimental results, a gasification model is developed.
The developed gasification model can predict the gasification rate and syngas generation of
different sized particles. A virtual gasification reactor was built based on the results found in
this research. The research can be extended by investigating the gasification rates of more
materials and a more accurate prediction of the performance of an existing gasification
reactor or one that is in the planning stage ascertained.
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