Flue gas desulfurization and mercury removal device and method
A flue gas and mercury removal technology, which is applied in the direction of separation methods, chemical instruments and methods, and mercury compounds, can solve the problems of high cost of flue gas desulfurization and mercury removal, achieve high desulfurization and mercury removal effects, simple devices, and improve costs Effect
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Embodiment 1
[0051] Taking the flue gas produced by a coal-to-liquid enterprise in Ningxia Hui Autonomous Region as the processing object, install an oxidation slurry spray device, a desulfurization slurry spray device, a hydrogen sulfide gas spray device and a bag filter in the chimney. The structure is as follows figure 1 As shown, where
[0052] The oxidizing slurry includes hypochlorous acid, sodium chloride, calcium bromide and water. The molar ratio of hypochlorous acid, sodium chloride and calcium bromide is 1:2:3, and the mass concentration of hypochlorous acid is 20%;
[0053] The desulfurization slurry includes calcium hydroxide, limestone and water, the weight ratio of calcium hydroxide to limestone is 3:2, and the mass concentration of calcium hydroxide is 20%;
[0054] The bag filter is provided with an adsorption packing layer of brominated activated carbon.
[0055] After stable operation, the average mercury removal rate of flue gas was 94.3%, and the average desulfurization rate w...
Embodiment 2
[0057] Taking the flue gas produced by a coal-to-liquid enterprise in Ningxia Hui Autonomous Region as the processing object, install an oxidation slurry spray device, a desulfurization slurry spray device, a hydrogen sulfide gas spray device and a bag filter in the chimney. The structure is as follows figure 1 As shown, where
[0058] The oxidizing slurry includes hypochlorous acid, sodium chloride, calcium bromide and water. The molar ratio of hypochlorous acid, sodium chloride and calcium bromide is 1:1.5:2.5, and the mass concentration of hypochlorous acid is 20%;
[0059] The desulfurization slurry includes calcium hydroxide, limestone and water, the weight ratio of calcium hydroxide to limestone is 2:1, and the mass concentration of calcium hydroxide is 20%;
[0060] The bag filter is provided with an adsorption packing layer of brominated activated carbon.
[0061] After stable operation, the average mercury removal rate of flue gas was 93.9%, and the average desulfurization ra...
Embodiment 3
[0063] Taking the flue gas produced by a coal-to-liquid enterprise in Ningxia Hui Autonomous Region as the processing object, install an oxidation slurry spray device, a desulfurization slurry spray device, a hydrogen sulfide gas spray device and a bag filter in the chimney. The structure is as follows figure 1 As shown, where
[0064] The oxidizing slurry includes hypochlorous acid, sodium chloride, calcium bromide and water. The molar ratio of hypochlorous acid, sodium chloride and calcium bromide is 1:2.5:3.5, and the mass concentration of hypochlorous acid is 20%;
[0065] The desulfurization slurry includes calcium hydroxide, limestone and water, the weight ratio of calcium hydroxide to limestone is 1:1, and the mass concentration of calcium hydroxide is 20%;
[0066] The bag filter is provided with an adsorption packing layer of brominated activated carbon.
[0067] After stable operation, the average mercury removal rate of flue gas was 92.5%, and the average desulfurization ra...
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