Process of producing cement clinker

Details Process of producing cement clinker Process of producing cement clinker

C - Chemistry, Metallurgy

04

B

261/62

C04B 7/36 (2006.01) C04B 7/43 (2006.01) F23C 10/00 (2006.01) F23C 10/10 (2006.01) F27B 7/20 (2006.01)

Patent

CA 1161072

ABSTRACT OF THE DISCLOSURE: In a process of producing cement clinker comprising preheating the raw cement powder in a suspension-type heat ex- changer, de-acidifying in a precalcining system, clinkering in a fluidized bed, and subsequently cooling the clinker, the improvement comprising: de-acidifying said raw cement powder at a temperature above 850°C to a degree of at least 95 % in a de-acidification circulation system comprising a de-acidifica- tion fluidized bed reactor, a cyclone separator and a recycling duct; feeding at least 65 % relative to the total heat require- ment, of the fuel required for the calcining and clinkering processes to the de-acidifying fluidized bed reactor and at least 10 %, relative to the total heat requirement to the clink- ering fluidized bed reactor. Then, near stoichiometrically burning the fuel supplied to the de-acidifying fluidized bed reactor in at least two combustion stages with at least two partial streams of oxygen-containing gas, one of said streams being supplied as fluidizing gas and the other being supplied on a higher level as secondary gas, the ratio of the rates and volumes of fluidizing gas to secondary gas being maintained in the range from 1:1 to 1:10 so that a mean suspension density of 100 to 300 kg/m3 is maintained in the zone between the inlet for fluidizing gas and the inlet for secondary gas; and main- taining a mean suspension density of 5 to 30 kg/m3 above the inlet for secondary gas.

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