Industrial process for the production of a clinker with a high content of belite
The present invention relates to a process for the production of a clinker with a high content of belite, said process comprising the following steps: (i) introducing a raw meal into a calcination chamber of a cement plant kiln; (ii) calcining the raw meal at a temperature of from 1150° C. to 1375° C.; (iii) measuring the weight per liter of the product of step (ii) and eliminating the product having a weight per liter strictly less than 650 g/liter; (iv) measuring the quantity of SO 3 in the product of step (ii) and eliminating the product having a ratio of quantity of SO 3 of the decarbonated raw meal/quantity of SO 3 in the product of step (ii) less than or equal to 0.75 and greater than or equal to 1.2; (v) measuring the quantity of free lime (CaOl) in the product of step (ii) and eliminating the product having a quantity of free lime strictly greater than 1.5%, percentage by mass of free lime in the product of step (ii).
1. A process for producing a clinker comprising 40 to 75% of belite, % by mass relative to the total mass of clinker, said process comprising:
(i) introducing a raw meal into a calcination chamber of a cement plant kiln;
(ii) calcining the raw meal at a temperature of from 1150° C. to 1375° C.;
(iii) measuring a weight per liter of the product of step (ii) and eliminating the product having a weight per liter strictly less than 650 g/liter;
(iv) measuring a quantity of SO 3 in the product of step (ii) and eliminating the product having a ratio of quantity of SO 3 of the decarbonated raw meal/quantity of SO 3 in the product of step (ii) less than or equal to 0.75 and greater than or equal to 1.2;
(v) measuring a quantity of free lime (CaOl) in the product of step (ii) and eliminating the product having a quantity of free lime strictly greater than 1.5%, percentage by mass of free lime in the product of step (ii).
2. The process according to claim 1 , wherein the raw meal introduced in step (i) comprises at least a source of calcium, a source of silica, a source of alumina, a source of iron, a source of sulphur, a source of boron.
3. The process according to claim 1 , comprising pre-calcinating the raw meal.
4. The process according to claim 1 , wherein step (i) is carried out in a rotary kiln or an electric kiln or a continuous kiln or any other type of cement plant kiln.
5. The process according to claim 1 , wherein in step (iv), the product of step (ii) having a ratio of quantity of SO 3 of the decarbonated raw meal/quantity of SO 3 in the product of step (ii) equal to 1 is not eliminated.
6. The process according to claim 1 , wherein in step (v), the product of step (ii) having a quantity of free lime strictly greater than 1% is eliminated, percentage by mass of free lime in the product of step (ii).