Method and plant for the production of cement clinker
The method according to the invention for producing cement clinker comprises substantially the following method steps: raw cement material is preheated in a preheater, the preheated material is heated further in a calcining zone while admitting combustion air, and the material heated in this manner is fired in a kiln to form cement clinker, wherein a part of the waste gases developing in the kiln is used to preheat the raw cement material in the preheater, and another part is diverted, and is used in a heat exchanger to preheat the combustion air used in the calcining zone.
1. A method for producing cement clinker, wherein
a. raw cement material is preheated in a preheater,
b. the preheated material is heated further in a calcining zone while admitting combustion air,
c. the material heated in this manner is fired in a kiln to form cement clinker,
d. wherein a part of the waste gases developing in the kiln is used to preheat the raw cement material in the preheater, and another part is diverted,
characterised in that at least a part of the diverted kiln waste gases is used in a heat exchanger to preheat the combustion air used in the calcining zone.
2. A method according to claim 1 , characterised in that the diverted part of the kiln waste gases is fed to a separator upstream of the heat exchanger.
3. A method according to claim 2 , characterised in that the diverted part of the kiln waste gases has a dust load that is separated in the separator and re-admitted to the kiln.
4. A method according to claim 1 characterised in that in the case of an increased amount of gas resulting from the use of alternative raw materials and/or fuels, the diverted flow is adjusted in terms of quantity in such a manner that the gas volume through the preheater remains constant.
5. A method according to claim 1 , characterised in that one or more of tertiary air of a cooler and ambient air is used as combustion air to be preheated.
6. A method according to claim 1 , characterised in that 75 to 95% by volume of the kiln waste gases are used in the preheater.
7. A method according to claim 1 , characterised in that the reduced energy input into the preheater resulting from the diverted part of the kiln waste gases is partially compensated by the capacity flow ratio between solid and gas and the associated increase in efficiency of the preheater and by the preheating of combustion air in the heat exchanger, in such a manner that the overall energy consumption for the production of the cement clinker is not increased.
8. A method according to claim 1 , characterised in that the one part of the kiln waste gases having a temperature of at least 830° C. is introduced into the preheater and the other part of the kiln waste gases having a temperature of at least 830° C. is diverted.
9. A method according to claim 1 , characterised in that the part of the kiln waste gases to be fed to the heat exchanger is diverted between the calciner and the preheater.