Low-nitrogen combustion type garbage incinerator and combustion method
A waste incinerator and waste incineration technology, applied in the direction of combustion method, incinerator, combustion type, etc., can solve the problems of high equipment cost, high cost, high operation and maintenance costs, and achieve good denitrification effect and simple structure
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Embodiment 1
[0049]In order to solve the problems existing in the prior art, the present invention provides a low-nitrogen burning garbage incinerator, which includes an incinerator 1, a first air extraction port 2, a first electric damper 3, and a second electric damper 4 , the second air extraction port 5, Venturi flowmeter 6, air duct main pipe 7, fan 8, temperature sensor 9, pressure sensor 10, third electric damper 11, nozzle header 12, nozzle 13 and secondary air nozzle 14.
[0050] The waste incinerator of the present invention will be further described below in conjunction with the accompanying drawings. First, the waste incinerator in the present invention at least includes a feed inlet, a feed grate, a fire grate for waste incineration in the furnace, and a fire grate located in the hearth. The primary air supply system at the lower part of the incinerator grate, the secondary air supply system at the throat of the furnace and the slag discharger. In addition, the garbage inciner...
Embodiment 2
[0062] The present invention also provides a combustion control method of a low-nitrogen combustion waste incinerator, said method comprising the following steps:
[0063] Step S1: Turn on the fan during the waste incineration process, so that the flue gas drawn from the first air extraction port at the tail of the waste incinerator enters the air duct main pipe;
[0064] Step S2: The flue gas is sprayed into the flue through the duct main pipe, and mixed with the flue gas in the flue to reduce the oxygen content in this area and suppress NO x The formation and reduction of part of NO x .
[0065] In the method, the excess air ratio of the incinerator should be controlled within the range of 1.4 to 1.65, and the ratio of the primary air to the secondary air is 8:2, and the amount of flue gas extracted from the first air extraction port 2 is the primary air volume 25%~35% of (in Nm 3 / h unit shall prevail).
[0066] Further, the first electric damper 3 is opened, the second...
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