Method of combustion or gasification in a circulating fluidized bed
AssigneeMG Technologies AG
InventorsWerner-Friedrich Staab, Wolfgang Pauly, Niels Henriksen
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AssigneeMG Technologies AG
InventorsWerner-Friedrich Staab, Wolfgang Pauly, Niels Henriksen
Estimating the term…
A material containing combustible components is burned or gasified in a circulating fluidized bed comprising a turbulence chamber, a solids separator connected to the upper area of the turbulence chamber, a return line leading from the solids separator to the turbulence chamber and a cooling device for the indirect cooling of solids arriving from the solids separator. The cooling device comprises several fluidized beds through which the solids pass one after the other. The first fluidized bed, into which the hot solids arriving from the solids separator are introduced first, is situated in a dechlorinating chamber. Fluidizing gas and at least one of the following dechlorinating additives: a) gaseous SO2 or a material which contains sulfur and releases SO2 in an oxidizing atmosphere, b) silicates and aluminium silicates, c) activated silicate, or d) other alkali-binding and HCl-releasing additives, are also introduced into the dechlorinating chamber in at least stoichiometric quantities so as to convert the alkali and metal chlorides contained in the arriving solids.
A method of combusting or gasifying material containing combustible components in a circulating fluidized bed which has a turbulence chamber for the combustion or gasification, a solids separator connected with the upper region of the turbulence chamber, a recycle from the solids separator of settled solids to the turbulence chamber and a cooling device for the indirect cooling of solids which come from the solids separator, in which the chlorine device includes several fluidized beds through which the solids migrate one after the other, characterized in that the first fluidized bed in which the hot solids arrive initially form the solids separator, whereby with fluidizing gas at temperatures in the range of 700 to 1100° C. and the presence of at least one dechlorination additive in the form of
Dependencies are inferred from the claim text.