The effect of coal particle agglomeration during pulverized coal combustion is studied using a plug-flow model of a practical coal combustor. The model incorporates turbulent agglomeration, in addition to the combustion equations, to explore certain combustor and coal parameters that may be used for
Opposed-flow combustion of pulverized coal
โ Scribed by Z. Hazanov; Y. Goldman; Y.M. Timnat
- Publisher
- Elsevier Science
- Year
- 1985
- Tongue
- English
- Weight
- 1010 KB
- Volume
- 61
- Category
- Article
- ISSN
- 0010-2180
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โฆ Synopsis
The possibility of achieving higher combustion intensity under conditions of stable burning by opposed-flow combustion is demonstrated in a series of experiments conducted in a furnace, provided for this purpose with an auxiliary combustion chamber. For this purpose measurements of temperature, pressure, gas composition, and velocity were carried out. Particle size distribution, ash, and volatile matter content were measured at the impingement point in order to determine locally the extent of the reaction and devolatilization. The results obtained regarding the burning of pulverized coal for the flow and temperature conditions actually existing in the combustion chamber were also analyzed computationally. The main advantages of the configuration investigated, in which secondary air is supplied in the final stage of the combustion process, are improved mixing of fuel and air and the ability to control the motion of the pulverized coal.
๐ SIMILAR VOLUMES
The reported combustion kinetics of pulverized coal from two types of experiments are compared: the first from measured rates of burnout at particle temperatures of 900-2200K and the second from an analysis based on the minimum gas temperatures at which coal ignites, corresponding to particle temper