Cement clinker and preparation method thereof
A technology of cement clinker and mixture, which is applied in the field of cement, can solve the problems of insufficient utilization, etc., and achieve the effects of weakening pipeline crust clogging, reducing cleaning times, and avoiding clogging
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[0030] A method for preparing cement clinker, comprising:
[0031] Mix limestone, copper slag, coal gangue and oil shale solid waste to obtain a mixture;
[0032] The mixture is conveyed for grinding, homogenization and then conveyed to the preheater for preheating. The temperature of the primary outlet of the preheater is 310-320°C;
[0033] After preheating, it is sent to the decomposition furnace for decomposition, and the outlet temperature of the decomposition furnace is lower than 860°C;
[0034] The materials decomposed by the calciner are transported to the rotary kiln for calcination, and the secondary air temperature of the rotary kiln is lower than 1250°C.
[0035] In the prior art, cement clinker is also prepared by using oil shale solid waste residue, limestone and other materials. However, during the preparation process, the pipeline and preheater will be blocked, and the chlorine ions and sulfate ions excluded from the decomposition furnace will be enriched in ...
Embodiment 1
[0061] The present embodiment provides a kind of cement clinker, mainly makes through the following steps:
[0062] The mixture of limestone, copper slag and coal gangue is pre-homogenized, and the oil shale solid waste is pre-homogenized; the mixed and pre-homogenized materials are grinded and homogenized to obtain a mixture.
[0063] The mixture is sent to the preheater for preheating, and the temperature of the primary outlet of the preheater is 310°C;
[0064] After preheating, it is sent to the calciner for decomposition, and the temperature at the outlet of the calciner is 850°C;
[0065] The materials decomposed by the calciner are transported to the rotary kiln for calcination, and the secondary air temperature of the rotary kiln is 1240°C.
[0066] The mixture calcined by the rotary kiln is transported to the grate cooler for cooling.
[0067] Among them, the mass ratio of limestone, copper slag, coal gangue and oil shale solid waste is 80:2:14.5:3.5.
[0068] The ...
Embodiment 2
[0070] The present embodiment provides a kind of cement clinker, mainly makes through the following steps:
[0071] The mixture of limestone, copper slag and coal gangue is pre-homogenized, and the oil shale solid waste is pre-homogenized; the mixed and pre-homogenized materials are grinded and homogenized to obtain a mixture.
[0072] The mixture is sent to the preheater for preheating, and the temperature of the primary outlet of the preheater is 320°C;
[0073] After preheating, it is sent to the calciner for decomposition, and the temperature at the outlet of the calciner is 855°C;
[0074] The materials decomposed by the calciner are transported to the rotary kiln for calcination, and the secondary air temperature of the rotary kiln is 1250°C.
[0075] The mixture calcined by the rotary kiln is transported to the grate cooler for cooling.
[0076] Among them, the mass ratio of limestone, copper slag, coal gangue and oil shale solid waste is 77:3:16:4.
[0077] Oil shal...
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