Composite mineralizers/fluxes for the production of alite/calcium sulfoaluminate clinkers
US-12503393-B2 · Dec 23, 2025 · US
US9598312B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9598312-B2 |
| Application number | US-201314388513-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 8, 2013 |
| Priority date | Mar 29, 2012 |
| Publication date | Mar 21, 2017 |
| Grant date | Mar 21, 2017 |
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Provided is a method for controlling a free lime content of a clinker by regulating the free lime content. Here the amount of sulfur trioxide resulting from fuel and the used amount of a fluorine-based mineralizer are regulated using the following Formulas (1) to (3), thereby controlling the free lime content (f.CaO) of the clinker. f.CaO=0.29×e (0.65×A) ( A=a ×SO 3 +b ) (1) a=0.0001×F+9.2×t−0.18×HM−9.2 (2) b=−0.0005×F−32.8×t−2.9×HM+28.4 (3) SO 3 is an amount of sulfur trioxide in the clinker; a is a coefficient satisfying Formula (2); b is a coefficient satisfying Formula (3); F is an amount of fluorine in the clinker; when a burning temperature is X° C., t=X/1450; and HM is a hydraulic modulus.
Opening claim text (preview).
The invention claimed is: 1. A method for controlling a free lime content of a cement clinker, comprising: adding fluorite or fluorine-containing waste that is a fluorine source in the cement clinker and used as a mineralizer to raw materials of the cement clinker, intermixing a waste gypsum board powder with fuel or putting the waste gypsum board powder into a kiln from the kiln outlet part as an SO 3 source in the cement clinker, burning the raw materials of the cement clinker added the fluorite or the fluorine-containing waste in the kiln to produce the cement clinker, calculating the free lime content (f.CaO) of the cement clinker according to Formulas (1) to (3), adjusting an additive amount of fluorite or fluorine-containing waste and an used amount of fuel or an additive amount of waste gypsum according to the calculated free lime content to control the free lime content (f.CaO) so as to fall within a range of 0.5<f.CaO<1.0, f.CaO=0.29 ×e (0.65×A) ( A=a ×SO 3 +b ) (1) a =0.0001 ×F +9.2 ×t −0.18 ×HM −9.2 (2) b =−0.0005 ×F −32.8 ×t +2.9 HM +28.4 (3) in Formula (1), f.CaO is a free lime content (wt %), SO 3 is an amount (wt %) of sulfur trioxide in the cement clinker, a is a coefficient satisfying Formula (2), b is a coefficient satisfying Formula (3), F is an amount (mg/kg) of fluorine in the cement clinker, t is a coefficient determined based on a temperature of 1450° C. (when a burning temperature is X° C., t=X/1450), and HM is a hydraulic modulus. 2. The method for controlling a free lime content of a cement clinker according to claim 1 , wherein the amount of fluorine in the cement clinker is equal to or greater than 300 mg/kg.
Condition or time responsive control in hydraulic cement manufacturing processes (controlling or regulating in general G05; F27B7/42 takes precedence) · CPC title
Oxides, Hydroxides · CPC title
Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel (fuels in general C10L); Use of particular energy sources, e.g. waste hot gases from other processes · CPC title
Inorganic materials · CPC title
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