Cement kiln system and cement clinker preparation method for realizing zero emission of carbon dioxide
A technology for cement clinker and carbon dioxide, which is applied in the treatment of discharged materials, cement production, carbon capture, etc., can solve the problems of low gas capture efficiency, low concentration, and high system investment and operation costs, and achieve a small system modification workload, Realization of zero discharge and improvement of capture efficiency
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Embodiment 1
[0061] like figure 1 As shown, the cement kiln system for realizing zero carbon dioxide emission in this embodiment includes a smoke chamber 1, a rotary kiln 2, a cooler 3, a fan 4, a raw meal preheating and pre-decomposition system, a first pipeline assembly and a second pipeline Road components, the raw meal preheating and pre-decomposition system is a conventional raw meal preheating and pre-decomposition system.
[0062] The raw meal preheating and pre-decomposition system communicates with the smoke chamber 1 , the rotary kiln 2 is provided with a first burner 201 , the tail of the rotary kiln 2 communicates with the smoke chamber 1 , and the head of the rotary kiln 2 communicates with the cooler 1 .
[0063] The raw meal preheating and pre-decomposition system includes a decomposition furnace 5 and a cyclone preheater. The cyclone preheater includes a first row of cyclone preheaters and a second row of cyclone preheaters. It should be noted that the row of cyclone prehea...
Embodiment 2
[0109] like figure 2 As shown, the cement kiln system for realizing zero carbon dioxide emission in this embodiment is basically similar in structure to the cement kiln system in Embodiment 1, except that the first waste heat utilization system in this embodiment includes a heat exchanger and a coal grinding device , that is, the first cooling gas of the third channel exchanges heat with the air through the heat exchanger, and the air after heat exchange enters the coal mill for drying, and then is discharged into the atmosphere after being treated with flue gas, and the gas after heat exchange is divided into The two routes enter the first branch pipeline 901 and the second branch pipeline 902 respectively.
[0110] The method for preparing cement clinker by adopting the cement kiln system in this embodiment is the same as that in Embodiment 1.
Embodiment 3
[0112] like image 3 As shown, the cement kiln system for realizing zero carbon dioxide emission of this embodiment is basically similar in structure to the cement kiln system of Embodiment 1, and the differences are as follows:
[0113] 1. The withstand temperature of the middle roller in the cooler 3 is greater than or equal to 900 °C, and the withstand temperature of the middle roller is greater than or equal to 900 °C. The roller is generally located in the front or middle of the cooler 3. At this time, the first cooling gas is divided into two way;
[0114] The first cooling gas of the first path directly enters the rotary kiln as secondary air for fuel combustion;
[0115] The first cooling gas of the second passage enters the decomposition furnace as tertiary air through the tertiary air duct for fuel combustion.
[0116]2. The other end of the fifth branch pipe 905 is mixed with pure oxygen to obtain a mixed gas of pure oxygen and high-concentration carbon dioxide ci...
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