Sewage storage tank exhaust air-release purification processing method
A technology for discharging gas and storage tanks, which is applied in the direction of heating water/sewage treatment, chemical instruments and methods, and separation methods. The effect of low running cost
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Embodiment 1
[0020] 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 side line extraction condensation of the stripping tower is three-stage condensation, wherein the weight concentration of the subcondensed liquid ammonia in the third-stage condensation is about 30%. The above-mentioned third-stage condensation and segregation liquid is used as the first-stage absorption liquid for the purification treatment of the exhaust gas of the acidic water storage tank. The absorbent is hydrorefined by catalytic cracking diesel fraction, and then the distillate oil at 250-360°C is distilled out. The kinematic viscosity of the absorbent at 40°C is 4mm 2 / s, freezing point -20°C.
[0021] Table 1 Concentration of main odor pollutants in the discharge gas of acidic water storage tanks
[0022] Main types of odor
[0023] The acid sewage storage tank adopts two-stage purification operation. The purific...
Embodiment 2
[0028] 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, and the weight concentration of ammonia is 20%. , liquid-gas ratio 12~15L / m 3 The diameter of the second-stage absorption tower is 700mm, and the height of the packing layer is 3500mm. The absorbent is distilled and separated from petroleum atmospheric distillate oil at 300-380°C. Distillate oil obtained from butylphenol (40°C kinematic viscosity is 30mm 2 / s, freezing point -5°C) or squalane (isotriacane), liquid-gas ratio 6-8L / 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 re...
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