A water-ammonia flue gas desulfurization and dust removal process
A technology for desulfurization, dust removal, and flue gas, which is applied in separation methods, ammonia compounds, gas treatment, etc., can solve the problems that the system cannot run for a long period, insufficient use of desulfurization agents, and insufficient gas-liquid contact, etc., to improve spray coverage High efficiency, good for defogging, and long residence time
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Embodiment 1
[0023] The desulfurization and dust removal device used in Example 1 includes: gas-gas heat exchanger 1, desulfurization tower 2, ejector 3, tubular first neutralization reactor 4, tubular second neutralization reactor 5, ammonia gas-liquid separator 6. Tubular oxidation reactor 7, oxidation liquid separator 8, chimney 9, connecting pipelines and intermediate tanks between equipment, gas delivery device, liquid delivery device, control and display instruments and meters and various accessories. Among them, the tubular first neutralization reactor 4, the tubular second neutralization reactor 5, and the tubular oxidation reactor 7 are composed of straight pipes and curved pipes in series, and chemical fillers are installed in the pipes; the water entering the desulfurization tower includes fresh water , ammonium sulfate crystallization and evaporation of water; the dilute acid solution in the tower kettle is partially circulated and returned to the desulfurization tower 2. Fresh...
Embodiment 2
[0025] Embodiment 2 is basically the same as Example 1, except that the first tubular neutralization reactor 4 used, the second tubular neutralization reactor 5, and the straight pipe part of the tubular oxidation reaction 7 are static mixers, The curved pipe part is an empty pipe, and the dilute acid solution in the second tower kettle of the desulfurization tower undergoes oxidation reaction first and then neutralization reaction. See flow chart figure 2 .
Embodiment 3
[0027] Embodiment 3 is basically the same as Embodiment 1, except that part of the oxidized liquid separated by the oxidation separator is circulated back to the tubular oxidation reactor 7 to participate in the oxidation reaction again. The schematic flow chart is shown in image 3 .
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