Waste heat furnace capable of adjusting sprayed urea and removing fly ash

Abstract

The invention discloses a waste heat furnace capable of adjusting sprayed urea and removing fly ash. The waste heat furnace comprises a waste heat furnace body; the waste heat furnace body comprises a plurality of boiler membrane type wall pipes and boiler membrane type wall fins located between every two adjacent boiler membrane type wall pipes; openings are formed in the boiler membrane type wall fins; a double-fluid spray gun is arranged on the outer side of the waste heat furnace body; the end, close to a spray nozzle, of the double-fluid spray gun penetrates through the openings; a compressed air atomization pipeline and a urea solution pipeline are arranged in the double-fluid spray gun, and the compressed air atomization pipeline and the urea solution pipeline communicate with each other; and a plurality of temperature measuring points are arranged in the waste heat furnace body, and the double-fluid spray gun moves according to the temperature of the temperature measuring points. The waste heat furnace can adjust sprayed urea and remove fly ash in the furnace.

Description

technical field [0001] The invention relates to the technical field of waste treatment machinery, in particular to a waste heat furnace capable of removing fly ash by adjustable injection of urea. Background technique [0002] Since hazardous waste contains nitrogen and the standard requires that the combustion temperature of the second combustion chamber stay at 1100°C for no less than 2 seconds, the nitrogen in the waste and the nitrogen in the combustion-supporting air will produce nitrogen oxides during high-temperature combustion. There are emission limit requirements for the emission value of nitrogen oxides in the norms, and the emission cannot exceed the standard. For this reason, it is necessary to spray urea solution near the boiler inlet position (flue gas temperature is 950°C), and the sprayed urea solution reacts with nitrogen oxides in the flue gas, thereby reducing nitrogen oxides to nitrogen and water, and as a flue gas. The composition of the gas is emitted...

AI Technical Summary

Problems solved by technology

When the flue gas flows through the cavity of the membrane wall, the dust in the flue gas will accumulate on the surface of the membrane wall, and as the running time increases, the deposited fly ash will gradually thicken, which will greatly reduce the heat transfer effect of the tube and reduce the temperature of the boiler. The heat exchange efficiency increases, the boiler exhaust temperature increases, resulting in waste of heat, and at the same time the boiler steam output decreases, reducing the benefits of the enterprise

The usual cleaning methods include vibration cleaning and shock wave cleaning. The structure of the membrane wall boiler is very strong, and vibration cleaning has no obvious effect. Due to the large volume of the cavity, the shock cleaning efficiency is low. It is also very limited. In addition, the flue gas from hazardous waste incineration is relatively viscous, and the fly ash has a certain viscosity, which increases the difficulty of ash cleaning. It is a common problem that the ash accumulation in hazardous waste incineration boilers is difficult to clean.

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