A method for recovery and utilization of waste heat in the process of light burning of magnesite
A waste heat recovery and magnesite technology, applied in the field of magnesite smelting, can solve the problems of not effectively utilizing light-burned magnesia products, not specifying the multi-stage preheating system process, heat loss, etc., so as to reduce heat energy and fuel. Consumption, the effect of reducing coal consumption
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Embodiment 1
[0020] like figure 1 As shown in the figure, firstly, the clean gas is passed into the burner of the magnesite calciner, and the hot flue gas generated by the combustion rapidly calcines the magnesite powder through the gas-solid action, and the product passes through the cyclone, and the obtained high-temperature light-burned powder is It is sent to the product cyclone heat exchanger, and the heat energy of the product is used to heat the air blown by the induced draft fan, and then the preheated air is passed to the burner of the magnesite calciner after filtering and dust removal to improve the combustion efficiency and the product cyclone heat exchange. The number of separators is 1, and the light-burned magnesium product after being filtered and dedusted and cooled by the product cyclone heat exchanger is transported to the storage tank; the high-temperature flue gas obtained by the cyclone separator is passed through the flue gas cyclone heat exchanger. The raw magnesite...
Embodiment 2
[0022] like figure 2 As shown in the figure, firstly, the clean gas is passed into the burner of the magnesite calciner, and the hot flue gas generated by the combustion rapidly calcines the magnesite powder through the gas-solid action, and the product passes through the cyclone, and the obtained high-temperature light-burned powder is It is sent to the product cyclone heat exchanger, and the heat energy of the product is used to heat the air blown by the induced draft fan, and then the preheated air is passed to the burner of the magnesite calciner after filtering and dust removal to improve the combustion efficiency and the product cyclone heat exchange. The number of separators is 1, and the light-burned magnesium product after being filtered and dedusted and cooled by the product cyclone heat exchanger is transported to the storage tank; the high-temperature flue gas obtained by the cyclone separator is passed through the flue gas cyclone heat exchanger. The raw magnesit...
Embodiment 3
[0024] like image 3 As shown in the figure, firstly, the clean gas is passed into the burner of the magnesite calciner, and the hot flue gas generated by the combustion rapidly calcines the magnesite powder through the gas-solid action, and the product passes through the cyclone, and the obtained high-temperature light-burned powder is It is sent to the product cyclone heat exchanger, and the heat energy of the product is used to heat the air blown by the induced draft fan, and then the preheated air is passed to the burner of the magnesite calciner after filtering and dust removal to improve the combustion efficiency and the product cyclone heat exchange. The number of separators is 2, and the light-burned magnesium product after being filtered and dedusted and cooled by the product cyclone heat exchanger is transported to the storage tank; the high-temperature flue gas obtained by the cyclone The raw magnesite powder is preheated, the number of flue gas cyclone heat exchang...
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