Wet-type desulfuration method for steel scoria with flue gas
A technology for wet desulfurization and steel slag, applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve the problems of difficult resource utilization of by-products, unfavorable utilization of gypsum by-products, and few application examples, so as to improve the utilization of steel slag efficiency, solving the effect of slow dissolution rate and improving economic benefits
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Embodiment 1
[0024] Such as figure 1 As shown, the SO of the imported sintering flue gas 2 It is in parallel contact with the absorption liquid. Sintering flue gas1(SO 2 600mg / m3) from the top of the absorption tower 2 into contact with the steel slag absorption liquid 3 and flow down to remove SO 2 The final purified flue gas 4 is discharged from the lower part of the tower and sent into the chimney 5 to be discharged to the atmosphere. Absorb SO in flue gas 2 The steel slag after absorbing the rich liquid 6 enters the solid-liquid separator 7, and the steel slag increasing solution 12 sent from the ultrasonic solubilizer 11 (wherein, iron and its oxides, inorganic matter content other than calcium and magnesium are relatively large, and the total content of calcium and magnesium content 45%, 200 mesh) after mixing, precipitation and separation to obtain the supernatant 13 into the steel slag absorption liquid storage tank 14, and then use the pump 15 to send it into the absorption t...
Embodiment 2
[0027] Technological process is basically the same as embodiment 1, and difference is that absorption tower 2 adopts countercurrent mode, as figure 2 shown. That is, the flue gas 1 enters from the lower part of the absorption tower 2, and in the process of rising, it contacts with the absorption liquid sprayed from the top of the tower in reverse flow to absorb SO in the flue gas. 2 The final purified flue gas 4 is discharged from the top of the tower and sent into the chimney 5 to be discharged into the atmosphere.
Embodiment 3
[0029] This embodiment is the process of Method 2, which is basically the same as that of Example 1, except that the absorption rich liquid is first precipitated and separated, and the obtained supernatant is mixed with the steel slag absorption rich liquid and recycled, such as image 3 shown. That is, the steel slag absorption rich liquid 6 discharged from the bottom of the absorption tower 2 enters the solid-liquid separator 7, the sediment 16 enters the dehydration system for processing, and the supernatant liquid 13 enters the steel slag absorption liquid storage tank 14, where it is mixed with the steel slag increasing solution as Steel slag absorption solution 3 is recycled.
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