Incineration method for salt-contained organic mixed waste liquid
A waste liquid and organic technology, applied in the field of waste liquid treatment, can solve the problems of low safety factor, complicated incineration method, low work efficiency, etc., and achieve the effects of high combustion efficiency, excellent treatment effect and short combustion time
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Embodiment 1
[0015] After the gas-solid separation of the salt-containing organic mixed waste liquid in the separation chamber, the blower and burner of the incinerator are turned on to make the temperature of the incinerator reach 992°C, and compressed air is introduced into the waste liquid, and the amount of compressed air introduced is controlled as 0.6L to atomize the waste liquid, and then put it into the waste liquid burner. The temperature of the high-temperature burner is 1900°C, and the burning time is 3s; adjust the wind force of the cooling air system in the incinerator, and control the temperature of the flue gas at the inlet of the waste heat boiler to 1150°C; Finally, the flue gas with a temperature of 260°C is put into the lye for desulfurization, and after passing through the decolorization and deodorization device, the purified flue gas is discharged. The compression pressure of the compressed air is 0.6MPa.
[0016] Through the operation method of this embodiment, the ch...
Embodiment 2
[0018] After the gas-solid separation of the salt-containing organic mixed waste liquid in the separation chamber, the blower and burner of the incinerator are turned on to make the temperature of the incinerator reach 1110°C, and compressed air is introduced into the waste liquid, and the amount of compressed air introduced is controlled as 0.6L to make the waste liquid atomized, and then put it into the waste liquid burner. The temperature of the high-temperature burner is 1150°C, and the incineration time is 5s; 1110°C; Finally, the flue gas with a temperature of 255°C is put into the lye for desulfurization, and after passing through the decolorization and deodorization device, the purified flue gas is discharged. The compression pressure of the compressed air is 0.6MPa.
[0019] Through the operation method of this embodiment, the chemical oxygen demand contained in the exhaust gas is reduced to 66mg / L, which meets the national emission standard.
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