Method and device for carbon reduction denitration of kiln flue gas
A denitration and flue gas technology, applied in the field of kiln flue gas, can solve the problems of waste of resources, failure to reach the temperature window, narrow effective temperature window, etc., and achieve the effects of no secondary pollution, improved production efficiency, and improved efficiency.
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Embodiment 1
[0054] The simulated flue gas temperature is 700°C, and the NO concentration is 700mg / Nm 3 , SO 2 Concentration 0.5%, O 2 Concentration 1%, flue gas volume 100Nm 3 / h, the simulated flue gas in the induced draft chamber enters the carbon reduction denitrifier through the induced draft fan, and the operating pressure of the partition wall is 120pa. Continue to complete the drying and firing of the products in the kiln, and then discharge them through the exhaust fan to measure the NO x concentration.
Embodiment 2
[0056] The simulated flue gas temperature is 700°C and the NO concentration is 500mg / Nm 3 , SO 2 Concentration 1%, O 2 Concentration 1%, flue gas volume 100Nm 3 / h, the simulated flue gas in the induced draft chamber enters the carbon reduction denitrifier through the induced draft fan, and the operating pressure of the partition wall is 200pa. Continue to complete the drying and firing of the products in the kiln, and then discharge them through the exhaust fan to measure the NO x concentration.
Embodiment 3
[0058] The simulated flue gas temperature is 800°C and the NO concentration is 700mg / Nm 3 , SO 2 Concentration 0.5%, O 2 Concentration 1%, flue gas volume 100Nm 3 / h, the simulated flue gas in the induced draft chamber enters the carbon reduction denitrifier through the induced draft fan, and the operating pressure of the partition wall is 120pa. Continue to complete the drying and firing of the products in the kiln, and then discharge them through the exhaust fan to measure the NO x concentration.
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