Flue gas desulfurization additive
A technology of additives and flue gas, applied in the separation of dispersed particles, chemical instruments and methods, separation methods, etc., can solve the problems of lack of activity of limestone desulfurizer, difficulty in achieving high-efficiency desulfurization, and large denaturation range, so as to shorten the desulfurization reaction time, Effects of reducing the amount of residue and reducing operating costs
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Embodiment 1
[0011] Get 22% sodium carbonate, 20% aluminum sulfate, 14% ferric oxide, 19% aluminum oxide, 5% sodium carboxymethyl cellulose, 16% silicon dioxide micropowder and 4% sodium polyacrylate constitutes the flue gas desulfurization additive, and the particle size of the silicon dioxide micropowder is 2 μm.
[0012] After testing, when the coal-fired boilers in thermal power plants are fully fired with high-sulfur coal and the power generation is at full load, low-sulfur coal is not burned, coal blending is not required, and the desulfurization tower SO 2 The inlet concentration is 8000mg / Nm 3 -12000 mg / Nm 3 . Under the condition that the amount of slurry supplied to the desulfurization tower is constant, after using the flue gas desulfurization additive of the present invention, the desulfurization tower SO 2 The outlet concentration is from 1600mg / Nm 3 —1800mg / Nm 3 down to 280mg / Nm 3 within.
Embodiment 2
[0014] Get 24% sodium carbonate, 22% aluminum sulfate, 12% ferric oxide, 17% aluminum oxide, 6% sodium carboxymethyl cellulose, 14% silicon dioxide micropowder and 5% sodium polyacrylate constitutes the flue gas desulfurization additive, and the particle size of the silicon dioxide micropowder is 4 μm.
[0015] After testing, when the coal-fired boilers in thermal power plants are fully fired with high-sulfur coal and the power generation is at full load, low-sulfur coal is not burned, coal blending is not required, and the desulfurization tower SO 2 The inlet concentration is 8000mg / Nm 3 -12000 mg / Nm 3 . Under the condition that the amount of slurry supplied to the desulfurization tower is constant, after using the flue gas desulfurization additive of the present invention, the desulfurization tower SO 2 The outlet concentration is from 1600mg / Nm 3 —1800mg / Nm 3 down to 200mg / Nm 3 within.
Embodiment 3
[0017] Get 26% sodium carbonate, 19% aluminum sulfate, 17% ferric oxide, 16% aluminum oxide, 4% sodium carboxymethyl cellulose, 15% silicon dioxide micropowder and 3% sodium polyacrylate constitutes the flue gas desulfurization additive, and the particle size of the silica micropowder is 5 μm.
[0018] After testing, when the coal-fired boilers in thermal power plants are fully fired with high-sulfur coal and the power generation is at full load, low-sulfur coal is not burned, coal blending is not required, and the desulfurization tower SO 2 The inlet concentration is 8000mg / Nm 3 -12000 mg / Nm 3 . Under the condition that the amount of slurry supplied to the desulfurization tower is constant, after using the flue gas desulfurization additive of the present invention, the desulfurization tower SO 2 The outlet concentration is from 1600mg / Nm 3 —1800mg / Nm 3 down to 240mg / Nm 3 within.
[0019] It can be seen that the desulfurization additive made according to the components...
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