A wet flue gas desulfurization method
A technology of wet flue gas desulfurization and alkali method, which is applied in separation methods, chemical instruments and methods, gas treatment, etc., can solve the problems of high operating costs, achieve low operating costs, high economic and environmental benefits, and good desulfurization effects Effect
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Embodiment 1
[0022] SiO in fly ash alkaline pre-desilication lye 2 The content is 20g / L, the caustic alkali concentration is 80g / L, and the amount of lime added is based on CaO / SiO 2 Added at 1.0, stirred and reacted at a temperature of 90°C for 60 minutes, then filtered and washed, the obtained active calcium silicate had a water content of 75%, and a sodium oxide content of 1.2%; the active calcium silicate was prepared by adding water Form a desulfurizing agent suspension slurry with a liquid-solid ratio of 4.0; pump the desulfurizing agent suspension slurry to a spray-type flue gas desulfurization tower for circulating spray desulfurization, and the SO in the flue gas 2 The content is 2000mg / Nm 3 , the flue gas temperature is 70°C, and the liquid-gas ratio is 7.0L / m 3 , The flue gas desulfurization rate exceeds 97%.
Embodiment 2
[0024] Low-grade bauxite with an aluminum-silicon ratio of 3.0 is subjected to roasting and pre-desilication treatment, and the SiO in the pre-desilication lye obtained 2 The content is 30g / L, the caustic alkali concentration is 100g / L, and the amount of lime added is based on CaO / SiO 2 Added at 1.30, stirred and reacted for 60 minutes at a temperature of 90°C, then filtered and washed, the water content of the obtained active calcium silicate was 65%, and the content of sodium oxide was 2.5%; the active calcium silicate was prepared by adding water Form a desulfurizing agent suspension slurry with a liquid-solid ratio of 13; pump the desulfurizing agent suspension slurry to a spray-type flue gas desulfurization tower for circulating spray desulfurization, and the SO in the flue gas 2 The content is 800mg / Nm 3 , the flue gas temperature is 75°C, and the liquid-gas ratio is 13L / m 3 , The flue gas desulfurization rate exceeds 98%.
Embodiment 3
[0026] Low-grade bauxite with an aluminum-silicon ratio of 3.5 is roasted and pre-desiliconized, and the SiO in the pre-desiliconized alkali solution 2 The content is 40g / L, the caustic alkali concentration is 150g / L, and the amount of lime added is based on CaO / SiO 2 1.10 was added, stirred and reacted for 60 minutes at a temperature of 90°C, and then filtered and washed. The obtained active calcium silicate had a water content of 65% and a sodium oxide content of 1.1%; the active calcium silicate was prepared by adding water. Form a desulfurizing agent suspension slurry with a liquid-solid ratio of 5.0; pump the desulfurizing agent suspension slurry to a spray-type flue gas desulfurization tower for circulating spray desulfurization, and the SO in the flue gas 2 The content is 1200mg / Nm 3 , the flue gas temperature is 65°C, and the liquid-gas ratio is 10L / m 3 , The flue gas desulfurization rate exceeds 98%.
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