Apparatus for thermal processing of raw materials in dust form
AssigneeKlockner-Humboldt-Deutz Aktiengesellschaft
InventorClaus Bauer
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AssigneeKlockner-Humboldt-Deutz Aktiengesellschaft
InventorClaus Bauer
Estimating the term…
In cement clinker production lines having calcinator connected upstream of the rotary kiln and equipped with a second firing, in order that the most complete possible burnup or residual burnup, favorable from the standpoint of thermal economy, of uncombusted fuel constituents such as, for example, CO and/or uncombusted residual carbon be enabled in the calcinator, and indeed in the case of calcinators without, but in particular with, a device for the reduction of the NO.sub.x component present in the furnace off-gas (rotary kiln off-gas and calcinator off-gas), a low-pressure-drop swirl chamber (33) is arranged in the calcination stage (17) in the region of its flow diversion, which swirl chamber has an opening (32) in its upper region for the tangential inlet of gas-solids suspension and a central opening (34) on its bottom for the discharge of the swirled gas-solids suspension, and in its interior a solids-free or solids-poor, temperature-controlled core zone (36) of elevated temperature can be maintained for the implementation of certain reactions.
Apparatus for thermal processing of raw materials, in dust form, in particular in the production of cement clinker from cement raw meal, said raw meal being thermally processed in a burning process by means of preheating, calcination, sintering and cooling, and the off-gas stream of the sintering stage and the exhaust air stream of the cooling stage from the clinker cooler being utilized separately or jointly for the calcination of the raw meal in the calcination stage (17), which is supplied with fuel, the gas-solids suspension in the calcination stage (17) being diverted and led into the lowermost cyclone (28) of the cyclone preheater for the purpose of separating the calcined raw meal (29) from the gas stream, a swirl chamber (33) being arranged in the calcination stage (17) in the region of its flow diversion with imparting of a swirl to the gas-solids suspension, characterized by the fact that the swirl chamber (33) exhibits an opening (32) in its upper region for the tangential inlet of all the gas-solids suspension and a central opening (34) on its bottom for the discharge of the swirled gas-solids suspension to said lowermost cyclone (28) via a gas-conveying pipe (35).
An apparatus for the production of cement clinker by thermal processing of cement raw meal in dust form through stages of preheating, calcinating, sintering and cooling, said apparatus including a cyclone preheater with a plurality of vertically offset cyclones (12-28), a sintering kiln (23) and a clinker cooler (24), and further comprising:
Dependencies are inferred from the claim text.