Iron smelting flue gas treatment method
A technology for flue gas treatment and flue gas, which is applied in the field of iron smelting flue gas treatment, and can solve the problems of low mercury removal efficiency
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Embodiment 1
[0015] A method for treating flue gas from iron smelting. First, a dust collector is used to remove dust from the flue gas, and then the SCR method is used to remove nitrogen oxides in the flue gas. After the nitrogen oxides are removed, the flue gas is sent to a desulfurization device. The flue gas is emptied, and there is a nozzle in the desulfurization device. While desulfurization, the nozzle sprays a mixture of hydrogen chloride and hypochlorous acid into the desulfurization device. The molar ratio of hydrogen chloride and hypochlorous acid is 5:3, and the desulfurization device A composite adsorbent is arranged at the outlet of the flue gas. The specific composition of the composite adsorbent is 60wt% activated carbon, 20wt% MCM-41 and 20wt% NaY type zeolite. The preparation method of the composite adsorbent is a mixing method.
Embodiment 2
[0017] A method for treating flue gas from iron smelting. First, a dust collector is used to remove dust from the flue gas, and then the SCR method is used to remove nitrogen oxides in the flue gas. After the nitrogen oxides are removed, the flue gas is sent to a desulfurization device. The flue gas is evacuated, and there is a nozzle in the desulfurization device. The mixed solution of hydrogen chloride and hypochlorous acid is sprayed from the nozzle into the desulfurization device at the same time as desulfurization. The molar ratio of hydrogen chloride and hypochlorous acid is 7:3, and the desulfurization device A composite adsorbent is arranged at the outlet of the flue gas, and the specific composition of the composite adsorbent is 50wt% activated carbon, 25wt% MCM-41 and 25wt% NaY type zeolite, and the preparation method of the composite adsorbent is a mixing method.
Embodiment 3
[0019] A method for treating flue gas from iron smelting. First, a dust collector is used to remove dust from the flue gas, and then the SCR method is used to remove nitrogen oxides in the flue gas. After the nitrogen oxides are removed, the flue gas is sent to a desulfurization device. The flue gas is evacuated, and there is a nozzle in the desulfurization device. While desulfurization, the nozzle sprays a mixture of hydrogen chloride and hypochlorous acid into the desulfurization device. The molar ratio of hydrogen chloride and hypochlorous acid is 8:5, and in the desulfurization device A composite adsorbent is arranged at the outlet of the flue gas, and the specific composition of the composite adsorbent is 50wt% activated carbon, 25wt% MCM-41 and 25wt% NaY type zeolite, and the preparation method of the composite adsorbent is a mixing method.
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