Abstract A process for producing cement comprises grinding of a mixture of raw components containing calcium chloride. The resulting raw mixture is subjected to calcination at a temperature within the range of from 1,000 to 1,100° C to produce a clinker which is then crushed at a temperature of from 900 to 1,100° C. The crushed clinker is fractionated at a temperature of from 1,000 to 1,100° C with a stream of the fuel combustion products at the speed thereof of from 6 to 30 m/sec. Two clinker fractions are thus obtained, namely: a fraction with a particle size of from 3 to 20 mm and a fraction with a particle size of from 0.1 to 3 mm. Each fraction is separately desalted at a temperature of from 900 to 1,100° C by way of contacting with a stream of the heating agent comprising the fuel combustion products. The resulting desalted clinker fractions are cooled and ground. The process for producing cement according to the present invention features stable conditions of the clinker desalting achieving the depth of the order of 1.5-2%.
A process for producing cement comprising grinding a mixture of starting components containing calcium chloride, calcining the raw mixture at a temperature within the range of between 1,000 and 1,100° C to form a clinker; crushing said clinker at a temperature within the range of between 900 and 1,100° C; fractionating the crushed clinker at a temperature of from 1,00 to 1,100° C by a stream of fuel combustion products at a speed of said stream of from 6 to 30 m/sec to produce two clinker fractions, said two fractions being a fraction with a particle size of 3 to 20 mm and a fraction with a particle size of 0.1 to 3 mm; separately desalting said clinker fractions at a temperature within the range of between 900 and 1,100° C by contacting said clinker fractions with a stream of fuel combustion products; cooling the desalted clinker, and grinding said cooled desalted clinker.
Claim 2
Dependent Claim
153 words
A process for producing cement comprising grinding a mixture of starting components containing calcium chloride, calcining the raw mixture at a temperature within the range of between 1,000 and 1,100° C to form a clinker; crushing said clinker at a temperature within the range of between 900 and 1,100° C; fractionating the crushed clinker at a temperature of from 1,00 to 1,100° C by a stream of fuel combustion products at a speed of said stream of from 6 to 30 m/sec to produce two clinker fractions, said two fractions being a fraction with a particle size of 3 to 20 mm and a fraction with a particle size of 0.1 to 3 mm; separately desalting said clinker fractions at a temperature within the range of between 900 and 1,100° C by contacting said clinker fractions with a stream of fuel combustion products; cooling the desalted clinker, and grinding said cooled desalted clinker.