Method and device for treating malodorous flue gas
A flue gas treatment and odor technology, applied in the field of environmental science, can solve problems such as inability to achieve effective breakthrough in treatment technology, strong odor and odor, and achieve the effects of minimum operating cost, low equipment cost, and compact structure.
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Embodiment 10
[0042] In the glutamic acid fermentation industry, the fermentation effluent formed after extraction of the product is rich in high SO 4 2- , high NH 3 -N, high COD. At present, organic-inorganic compound fertilizers are produced by spraying and granulating the fermentation waste liquid at 550°C after being concentrated, so that the fermentation waste liquid can be recycled. However, under high temperature conditions, the organic matter in the fermentation waste liquid is cracked The formation of organic aerosol substances, VOCs, SVOCs, and water vapor together form the spray granulation malodorous smoke. In this example, 100,000 m 3 / h Malodorous flue gas treatment equipment as an example:
[0043] A malodorous flue gas treatment device is composed of two parts: an organic aerosol particle pollutant separation part, and a VOCs and SVOCs molecular decomposition part.
[0044] The structure of the organic aerosol particle pollutant separation part is as follows: it includes...
Embodiment 2
[0056] Other is with embodiment 1, and difference is:
[0057]The conductive anode tube group is composed of a number of anode tubes arranged in parallel, and the shape is a round tube honeycomb type, and the diameter of the round tube honeycomb type is 300-400mm;
[0058] The hydrogen peroxide reaction liquid sprayer is a primary spray, and the spray liquid is hydrogen peroxide (H 2 o 2 ); the acidic reaction liquid sprayer is a secondary spray, and the spray liquid is a hydrochloric acid reaction liquid with a pH value of 4; the alkaline solution sprayer is a three-stage spray, and the spray liquid is calcium hydroxide with a pH value of 10 solution.
[0059] The gas velocity of the pores of the secondary reaction layer sieve plate is 15m / s; the gas velocity of the pores of the primary reaction layer sieve plate is 18m / s.
[0060] The iron-carbon filler is made of iron-carbon micro-electrolytic material, and the components of the iron-carbon micro-electrolytic material ar...
Embodiment 3
[0062] Other is with embodiment 1, and difference is:
[0063] The hydrogen peroxide reaction liquid sprayer is a primary spray, and the spray liquid is hydrogen peroxide (H 2 o 2 ); the acidic reaction liquid sprayer is a secondary spray, and the spray liquid is a nitric acid reaction liquid with a pH value of 5; the alkaline solution sprayer is a three-stage spray, and the spray liquid is an ammonia solution with a pH value of 8.
[0064] The gas velocity of the pores of the secondary reaction layer sieve plate is 20m / s; the gas velocity of the pores of the primary reaction layer sieve plate is 22m / s.
[0065] The iron-carbon filler is made of iron-carbon micro-electrolytic material, and the components of the iron-carbon micro-electrolytic material are: iron filings: activated carbon: rare earth metal: clay=85%: 13.8%: 0.2%: 1%, all % by mass; the diameter of the iron-carbon micro-electrolytic filler is 3.0 cm. The rare earth metal includes Pr, and the rare earth metal is...
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