A device and method for photocatalytic oxidation removal of multiple pollutants in flue gas
A catalytic and pollutant-promoting technology, applied in the field of flue gas purification, can solve problems such as poor water solubility and low denitrification efficiency
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Embodiment 1
[0071] Compound oxidant solution: H 2 o 2 The mass concentration is 50wt%, and the pH is 6.
[0072] The above-mentioned liquid-phase composite oxidant is injected into the flue gas waste heat utilization and atomization generating device 2, and after passing through the photocatalytic activation reaction device 3 and the absorption device 5, the integrated desulfurization, denitrification and mercury removal are realized. The reaction conditions are shown in Table 2.
[0073] Table 2
[0074] Reaction conditions
[0075] According to the above conditions, the flue gas is desulfurized, demercurized and denitrified, and it is detected that: SO 2 The removal efficiency is 100%, the denitrification efficiency is 87%, and the mercury removal efficiency is over 92.1%.
Embodiment 2
[0077] Compound oxidant solution: H 2 o 2 The mass concentration ratio of NaBr and NaBr is 40:0.05, and the pH is 5.5.
[0078] The above-mentioned liquid-phase composite oxidant is injected into the flue gas waste heat utilization and atomization generating device 2, and after passing through the photocatalytic activation reaction device 3 and the absorption device 5, the integrated desulfurization, denitration and demercuration is realized. The reaction conditions are shown in Table 3.
[0079] table 3
[0080]
[0081]
[0082]According to the above conditions, the flue gas is desulfurized, demercurized and denitrified, and it is detected that: SO 2 The removal efficiency is 99%, the denitrification efficiency is 88.7%, and the mercury removal efficiency is over 94.7%.
Embodiment 3
[0084] Compound oxidant solution: H 2 o 2 The mass concentration ratio of NaCl and NaCl is 40:0.5, and the pH is 5.
[0085] The above-mentioned liquid-phase composite oxidant is injected into the flue gas waste heat utilization and atomization generating device, and after passing through the photocatalytic activation reaction device and the absorption device, the integrated desulfurization, denitrification and demercuration are realized. The reaction conditions are shown in Table 4.
[0086] Table 4
[0087]
[0088]
[0089] According to the above conditions, the flue gas is desulfurized, demercurized and denitrified, and it is detected that: SO 2 The removal efficiency is 99%, the denitrification efficiency is 86.4%, and the mercury removal efficiency is over 93.5%.
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