A method for simultaneous desulfurization and denitrification of aeration flue gas
An aeration type, flue gas technology, applied in the field of flue gas desulfurization and denitrification, can solve the problems of high cost of flue gas denitrification, and achieve the effects of easy automatic control, energy saving and cost reduction
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specific Embodiment approach 1
[0009] Specific implementation mode 1: This implementation mode is a method for simultaneous desulfurization and denitrification of aeration flue gas, which is specifically completed according to the following steps:
[0010] The electrolysis device is used as the absorption tower, and the mass fraction of 0.1% to 20% persulfate aqueous solution is used as the electrolyte. The aeration head is installed at the bottom of the electrolysis device, and the voltage applied to the anode of the electrolysis device is 1.8V to 1000V. At 100°C, the flue gas is injected into the electrolysis device through the aeration head, and the aeration speed is 0.1m 3 min -1 m -2 ~100m 3 min -1 m -2 , after desulfurization and denitrification, the flue gas is discharged from the upper part of the electrolysis device, and the electrolyte solution absorbing sulfur and nitrogen is sent to the centrifuge device, and then the precipitant is added to the centrifuge device, centrifuged, the precipitat...
specific Embodiment approach 2
[0011] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the precipitation agent is a salt containing metal cations, wherein the metal cations are calcium ions, potassium ions or a mixture of calcium ions and potassium ions. Others are the same as the first embodiment.
specific Embodiment approach 3
[0012] Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that the molar ratio of the S element in the electrolyte absorbing sulfur and nitrogen to the metal cation in the precipitant is 1:(0.3~5) . Others are the same as those in Embodiment 1 or 2.
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