Method for simultaneously removing SO2 and NO in flue gas by biological reduction and complexing absorption
A complex absorption and SO32- technology, which is applied in the field of flue gas purification, can solve the problems that the recycling of absorption liquid cannot be realized, hinder the application of technology, and difficult to regenerate, so as to achieve comprehensive treatment, no secondary pollution, investment and operating costs. less effect
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Embodiment 1
[0024] A 75t / h coal-fired thermoelectric boiler with a flue gas flow rate of 100,000 Nm 3 / h,SO 2 The content is 1000mg / Nm 3 , NO content is 500mg / Nm 3 , the flue gas temperature is 130°C, according to the process of the present invention, when leaving the absorption tower, the SO in the absorption tail gas 2 Content 100mg / Nm 3 , NO content is 75mg / Nm 3 , the desulfurization efficiency is 90%, and the denitrification efficiency is 85%.
[0025] The absorption tower is a spray tower with a diameter of 3.5m, a height of 22m, and a liquid-gas ratio of 6L / Nm 3 , the residence time of the absorption liquid in the circulating reaction pool is 5min, the desulfurization alkaline absorption liquid is prepared with NaOH during the absorption process, and the denitrification complexing agent is Fe II (EDTA).
[0026] The anaerobic bioreactor is an upflow anaerobic reactor UASB, the pH value is controlled at 7.0, the temperature is controlled at 32°C, and the residence time is 30 h...
Embodiment 2
[0029] A 220t / h coal-fired thermoelectric boiler with a flue gas flow rate of 250,000 Nm 3 / h,SO 2 The content is 800mg / Nm 3 , NO content is 400mg / Nm 3 , the flue gas temperature is 150°C, according to the process of the present invention, when leaving the absorption tower, the SO in the absorption tail gas 2 Content 80mg / Nm 3 , NO content is 60mg / Nm 3 , the desulfurization efficiency is 90%, and the denitrification efficiency is 85%.
[0030] The absorption tower is a spray tower with a diameter of 6m, a height of 25m, and a liquid-gas ratio of 6L / Nm 3 , the residence time of the absorbing liquid in the circulating reaction pool is 5min, and the desulfurization alkaline absorbing liquid in the absorption process uses Na 2 CO 3 Preparation, the denitrification complexing agent is Fe II (NTA).
[0031] The anaerobic bioreactor is an upflow anaerobic reactor UASB, the pH value is controlled at 7.0, the temperature is controlled at 35°C, and the residence time is 28 hour...
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