A method for simultaneously removing high-load sulfur dioxide and nitrogen oxides from waste gas
A technology for sulfur dioxide and nitrogen oxides, applied in chemical instruments and methods, separation methods, gas treatment, etc., can solve the problems of low removal rate and low concentration of nitrogen oxides, and achieve the effect of improving removal efficiency
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Embodiment 1
[0046] The exhaust gas in this embodiment comes from the simulated flue gas generated by the gas generating device. Before entering the synchronous desulfurization and denitrification packed tower, the simulated flue gas is first passed into the mixing device to mix the simulated flue gas with air.
[0047] Such as figure 1 As shown, the biofilm packing tower inlet 1, gas flow meter 2, intake pipeline 3, packing container 4, nutrient solution spraying device 5, exhaust Air port 6 , nutrient solution inflow pipeline 7 , peristaltic pump 8 , nutrient solution storage container 9 and nutrient solution outflow pipeline 10 .
[0048] The air inlet 1 is used for waste gas to enter the packed tower, and the gas is passed through the air inlet 1, and enters the packing container 4 of the packed tower through the air inlet line 3, and the process is passed through the air inlet line 3 The gas flow meter 2 on the top regulates the gas flow rate, and the generated gas is discharged thro...
Embodiment 2
[0057] This embodiment is basically the same as Embodiment 1, the difference is:
[0058] The concentration of sulfur dioxide at the air inlet 1 in this embodiment is 2850-3050mg / m 3 , the concentration of nitrogen oxides is 2150~2230mg / m 3 , The molar concentration ratio of sulfur dioxide and nitrogen oxides in the exhaust gas is 0.76:1.
[0059] The filler is ceramsite with a diameter of 200mm, and the desulfurization and denitrification treatment described in step 2) is carried out under an aerobic environment, and the aerobic environment is provided by air, and the oxygen concentration in the air is 20%. The flow is kept at 0.2m 3 / h, the gas residence time is 110 seconds, and the liquid-gas ratio is 40L / m 3 .
[0060] The operating temperature of the packed tower is 35°C.
[0061] After running for 2 cycles, detect the concentration of sulfur dioxide and nitrogen oxides in the exhaust gas at the outlet; after testing, the concentration of sulfur dioxide at the 6 outlet...
Embodiment 3
[0063] This embodiment is basically the same as Embodiment 1, the difference is:
[0064] The concentration of sulfur dioxide at the air inlet 1 in this embodiment is 2930-3000mg / m 3 , the concentration of nitrogen oxides is 1680~2000mg / m 3 , The molar concentration ratio of sulfur dioxide and nitrogen oxides in the exhaust gas is 1.06:1.
[0065] The filler is a porous acid-resistant plastic material with a diameter of 100mm, and the desulfurization and denitrification treatment in the step 2) is carried out in an aerobic environment, the aerobic environment is provided by air, and the oxygen concentration in the air is 20 %, set the air flow to keep at 0.2m 3 / h, the gas residence time is 110 seconds, and the liquid-gas ratio is 40L / m 3 .
[0066] The operating temperature of the packed tower is 30°C.
[0067] After running for 2 cycles, detect the concentration of sulfur dioxide and nitrogen oxides in the exhaust gas at the outlet; after testing, the concentration of s...
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