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- W82373885 abstract "A mathematical model is developed for coal char combustion with sulfur retention by limestone or dolomite in a gas fluidized bed employing noncatalytic single pellet gas-solid reactions. The shrinking core model is employed to describe the kinetics of chemical reactions taking place on a single pellet whose changes in size as the reaction proceeds are considered. The solids are assumed to be in back-mix condition whereas the gas flow is regarded to be in plug flow. The model is strictly valid for the turbulent regime where the gas flow is quite high and classical bubbles do not exist. Formulation of the model includes setting up heat and mass balance equations petaining to a single particle exposed to a varying reactant concentration along the height of the bed with accompanying changes in its size during the course of reaction. These equations are then solved numerically to account for particles of all sizes in the bed to obtain the overall carbon conversion efficiency and resultant sulfur retention. In particular, the influence of several fluid-bed variables such as oxygen concentration profile, additive particle size, reaction rate for sulfation reaction, sulfur absorption efficiency are examined on additive requirement." @default.
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- W82373885 date "1981-09-21" @default.
- W82373885 modified "2023-09-24" @default.
- W82373885 title "Modeling of Fluidized Bed Combustion of Coal Char Containing Sulfur" @default.
- W82373885 doi "https://doi.org/10.1021/bk-1981-0168.ch007" @default.
- W82373885 hasPublicationYear "1981" @default.
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