Technics of flue gas desulfurizing through catalytic oxidation method and by-product polymerizing iron sulfate through catalytic method
A technology of polymerizing ferric sulfate and catalytic oxidation, which is applied in the field of flue gas purification, can solve the problems of incomplete oxidation of ferrous ions, high price of oxidants, difficulty in popularization and application, etc., to achieve increased added value, increased oxidation rate, and obvious economic benefits Effect
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Embodiment 1
[0037] A 75t / h coal-fired thermoelectric boiler with a flue gas flow rate of 100,000 Nm 3 / h, SO 2 The content is 1500mg / Nm 3 , the flue gas temperature is 130°C, according to the process of the present invention, when leaving the desulfurization tower, the SO in the desulfurization tail gas 2 Content 150mg / Nm 3 , the flue gas temperature is 50°C, and the desulfurization efficiency is 90%.
[0038] The desulfurization tower is a packed tower with a diameter of 7m and a height of 28m. The packing is a stepped ring made of reinforced polypropylene with a nominal diameter of 50mm
[0039] The gas residence time of the desulfurization tower is 13s
[0040] The liquid-gas ratio of the desulfurization tower is 10L / Nm 3 , absorption liquid flow rate 1000m 3 / h
[0041] The oxidation tower is a bubble tower, and the liquid residence time is 20min
[0042] The catalytic synthesis tower is a packed tower with a diameter of 3.5m and a height of 6m. The filler is a stepped ring ma...
Embodiment 2
[0054] A 220t / h coal-fired thermoelectric boiler with a flue gas flow rate of 250,000 Nm 3 / h, SO 2 The content is 1500mg / Nm 3 , the flue gas temperature is 130°C, according to the process of the present invention, when leaving the desulfurization tower, the SO in the desulfurization tail gas 2 Content 150mg / Nm 3 , the flue gas temperature is 50°C, and the desulfurization efficiency is 90%.
[0055] The desulfurization tower is a packed tower with a diameter of 9.5m and a height of 32m. The packing is a stepped ring made of reinforced polypropylene with a nominal diameter of 50mm
[0056] The gas residence time of the desulfurization tower is 13s
[0057] The liquid-gas ratio of the desulfurization tower is 10L / Nm 3 , absorption liquid flow rate 2500m 3 / h
[0058] The oxidation tower is a bubble tower, and the liquid residence time is 20min
[0059] The catalytic synthesis tower is a packed tower with a diameter of 5m and a height of 7m. The filler is a stepped ring m...
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