Cleaning treatment method of acid sewage storage tank discharging gas
A technology for acidic sewage and gas discharge, applied in the direction of heating water/sewage treatment, chemical instruments and methods, separation methods, etc., can solve the problems of high operating costs and complicated processes, and achieve the effect of low operating costs and simple equipment
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Embodiment 1
[0018] An enterprise's sour water storage tank emits about 1000m3 of gas 3 / h, the composition of main odor pollutants is shown in Table 1. The extraction and condensation of the side line of the stripper is 3-stage condensation, in which the weight concentration of the condensed liquid ammonia in the third stage of condensation is about 30%, the concentration of hydrogen sulfide in the purified water by stripping is 5-15 mg / L, and the concentration of ammonia is 20-50 mg / L. The above two liquids are used as the absorption liquid for the purification treatment of the exhaust gas of the acidic water storage tank.
[0019] Table 1 Concentration of main odor pollutants in the discharge gas of acidic water storage tanks
[0020] Main types of odor
Odor species concentration (mg / m 3 )
100~12000
[0021] Main types of odor
Odor species concentration (mg / m 3 )
organic sulfide
10~2000
ammonia
...
Embodiment 2
[0026] According to the method described in Example 1, wherein the filler adopts Dg38 stainless steel saddle ring. The diameter of the first-stage eluting tower is 600mm, and the height of the packing layer is 2600mm. The eluent comes from the acidic water stripping ammonia gas condensate system, which is a mixed solution of the second-stage condensate and the third-stage condensate. , liquid-gas ratio 6~8L / m 3 ; The diameter of the second-stage elutriation tower is 700mm, the height of the packing layer is 3500mm, the eluent is stripped purified water, and the liquid-gas ratio is 12-15L / m 3 . The operating temperature of the first-stage rinsing and the second-stage rinsing is controlled at 35°C to 45°C. The eluent of the first-stage packed tower is recycled in the tower, and when the pH value of the eluent drops to 9, a new fractionated condensate is added. The eluent of the second-stage packed tower is not circulated. The effluent from both the first stage rinse and the ...
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