Integrative coordinated desulfurization, denitration, demercuration device and technique using spray bubbling method
A bubbling and denitrification technology, applied in separation methods, chemical instruments and methods, separation of dispersed particles, etc., can solve the problems of high investment and operation costs
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Embodiment 1
[0031] The integrated synergistic desulfurization, denitrification, and mercury removal absorption liquid of the present invention includes a limestone slurry with a mass concentration of 5%, and KMnO is added to the limestone slurry 4 , its addition is 0.02% of the limestone slurry quality, the technical scheme described in the present embodiment, when flue gas flow rate is 5000Nm 3 / h, SO 2 The concentration is 5000mg / Nm 3 , NO concentration is 1500mg / Nm 3 At this time, the flue gas desulfurization efficiency can reach more than 60%, the denitrification efficiency can reach more than 30%, and the elemental zero-valent mercury Hg 0 The removal efficiency can reach more than 40%.
Embodiment 2
[0033] The integrated synergistic desulfurization, denitrification, and mercury removal absorption liquid of the present invention includes a limestone slurry with a mass concentration of 20%, and KMnO is added to the limestone slurry 4 , its addition is 0.15% of the limestone slurry mass, the technical scheme described in this embodiment, when the flue gas flow rate is 1 × 10 6 N m 3 / h, SO 2 The concentration is 5000mg / Nm 3 , NO concentration is 1500mg / Nm 3 At this time, the flue gas desulfurization efficiency can reach more than 85%, the denitrification efficiency can reach more than 60%, and the elemental zero-valent mercury Hg 0 The removal efficiency can reach more than 70%.
Embodiment 3
[0035] The integrated synergistic desulfurization, denitrification, and mercury removal absorption liquid of the present invention includes a limestone slurry with a mass concentration of 30%, and KMnO is added to the limestone slurry 4 , its addition is 0.25% of the limestone slurry mass, the technical scheme described in this embodiment, when the flue gas flow rate is 1 × 10 6 N m 3 / h, SO 2 The concentration is 5000mg / Nm 3 , NO concentration is 1500mg / Nm 3 At this time, the flue gas desulfurization efficiency can reach more than 95%, the denitrification efficiency can reach more than 80%, and the elemental zero-valent mercury Hg 0 The removal efficiency can reach more than 90%.
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