Method for optimizing SNCR (selective non-catalytic reduction) denitrification system of garbage incinerator by adding anionic surfactant
A technology of surfactant and waste incinerator, which is applied in the field of SNCR denitrification of waste incinerator, can solve the problems such as unfavorable promotion and use of waste incineration power station, increase the difficulty of technical process, etc., and achieve the reaction efficiency and time, low price and improved efficiency Effect
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Embodiment 1
[0027] Embodiment 1: Adding anionic surfactant to optimize the method of SNCR denitrification system of waste incinerator
[0028] 1) Mix and dilute the ammonia water from the ammonia delivery module and the soft water from the soft water delivery module in the dilution module;
[0029] 2) At the same time, the required dose of sodium lauryl polyoxyethylene ether sulfate (SLES) is delivered to the dilution module described in step 1) under the control of the calculation module, so that the anionic surfactant added to the ammonia water during the dilution process; A mixed solution of ammonia water was obtained after mixing, the temperature was 28°C, the mass fraction of ammonia water in the mixed solution was 18wt%, and the mass fraction of SLES was 0.5 wt %;
[0030] 3) Under the control of the ammonia injection module, the above ammonia-water mixed solution is sent to the furnace through compressed air (at a temperature of 21°C) for denitrification reaction with flue gas; 6 ...
Embodiment 2
[0036] Embodiment 2: Adding anionic surfactant to optimize the method of SNCR denitrification system of waste incinerator
[0037] 1) Mix and dilute the ammonia water from the ammonia delivery module and the soft water from the soft water delivery module in the dilution module;
[0038] 2) At the same time, the required dose of sodium lauryl polyoxyethylene ether sulfate (SLES) is delivered to the dilution module described in step 1) under the control of the calculation module, so that the anionic surfactant added to the ammonia water during the dilution process; A mixed solution of ammonia water was obtained after mixing, the temperature was 28°C, the mass fraction of ammonia water in the mixed solution was 18wt%, and the mass fraction of SLES was 1 wt %;
[0039] 3) Under the control of the ammonia injection module, the above ammonia-water mixed solution is sent to the furnace through compressed air (at a temperature of 21°C) for denitrification reaction with flue gas; 6 g...
Embodiment 3
[0045] Embodiment 3: Adding anionic surfactant to optimize the method of SNCR denitrification system of waste incinerator
[0046] 1) Mix and dilute the ammonia water from the ammonia delivery module and the soft water from the soft water delivery module in the dilution module;
[0047] 2) At the same time, the required dose of sodium lauryl polyoxyethylene ether sulfate (SLES) is delivered to the dilution module described in step 1) under the control of the calculation module, so that the anionic surfactant added to the ammonia water during the dilution process; After mixing, the ammonia water mixed solution was obtained, the temperature was 28°C, the mass fraction of ammonia water in the mixed solution was 18wt%, and the mass fraction of SLES was 2wt%;
[0048] 3) Under the control of the ammonia injection module, the above ammonia-water mixed solution is sent to the furnace through compressed air (at a temperature of 21°C) for denitrification reaction with flue gas; 6 gro...
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