Flue gas desulfurization method
A flue gas and desulfurization tower technology, applied in the field of flue gas desulfurization, can solve the problems of low desulfurization efficiency
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Embodiment 1
[0045] The flue gas is first passed into the first desulfurization tower, the desulfurization agent in the first desulfurization tower is methyl aniline, the desulfurization temperature is 60°C, and the flow rate of the flue gas is 1000m 3 / h, the flow rate of methylaniline is 30m 3 / h; and store the treated flue gas in the gas storage tank. The flue gas in the gas storage tank is passed into the second desulfurization tower, the second desulfurization tower is equipped with activated carbon with a pore size of 1.5nm, the desulfurization temperature is 30°C, and the flue gas flow rate is 110m 3 / h, the replacement frequency of activated carbon is 2 times / h and the treated flue gas is stored in the gas storage tank. Finally, the gas in the processing pipe is passed into the third desulfurization tower, the desulfurization agent in the third desulfurization tower is sodium hydroxide solution, the mass ratio of sodium hydroxide to water in the sodium hydroxide solution is 3:1, an...
Embodiment 2
[0048] The flue gas is first passed into the first desulfurization tower, the desulfurizer in the first desulfurization tower is monoethanolamine, the desulfurization temperature is 50°C, and the flow rate of the flue gas is 1300m 3 / h, the flow rate of monoethanolamine is 80m 3 / h; and store the treated flue gas in the gas storage tank. The flue gas in the gas storage tank is passed into the second desulfurization tower, the second desulfurization tower is equipped with limestone with a pore size of 0.8nm, the desulfurization temperature is 50°C, and the flue gas flow rate is 145m 3 / h, the replacement frequency of limestone is 3 times / h and the treated flue gas is stored in the gas storage tank. Finally, the gas in the processing pipe is passed into the third desulfurization tower. The desulfurization agent in the third desulfurization tower is sodium carbonate solution. The mass ratio of sodium carbonate to water in the sodium carbonate solution is 6:1, and the desulfuriza...
Embodiment 3
[0051] The flue gas is first passed into the first desulfurization tower, the desulfurizers in the first desulfurization tower are monoethanolamine and diethanolamine, the desulfurization temperature is 80°C, and the flow rate of flue gas is 1500m 3 / h, the flow rate of monoethanolamine and diethanolamine is 50m 3 / h; and store the treated flue gas in the gas storage tank. The flue gas in the gas storage tank is passed into the second desulfurization tower, the second desulfurization tower is equipped with activated carbon and iron oxide with a pore size of 1nm, the desulfurization temperature is 40°C, and the flue gas flow rate is 160m 3 / h, the replacement frequency of activated carbon and iron oxide is 4 times / h and the treated flue gas is stored in the gas storage tank. Finally, the gas in the processing pipe is passed into the third desulfurization tower, the desulfurizing agent in the third desulfurization tower is basic aluminum sulfate solution, the mass ratio of basi...
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Abstract
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