Simulation study on desulfurization of sintering flue gas in a dense flow absorber
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摘要: 應用Fluent軟件對密相干塔模擬仿真,研究了煙氣整流系統和鏈式攪拌器對煙氣流場和湍流、循環灰軌跡及系統壓力損失的影響,并在模擬工況下確定了煙氣整流系統較優導流板布置形式.研究結果表明,鏈式攪拌器能夠顯著增大塔內附近區域的湍動能,提高轉速不能明顯提高整體煙氣湍流強度,雙層鏈式攪拌器可以增大高湍流強度區且減緩其衰減速度,該工況下安裝雙層鏈式攪拌器,轉速為100 r·min-1較為理想,此時密相干塔能夠實現煙氣均布和氣固充分接觸,大部分顆粒參與內循環,少部分進入除塵器,系統壓損約為200 Pa.Abstract: A numerical simulation of a dense flow absorber with Fluent software was performed to study the effects of the flue gas rectifier system and the chain agitator on the flow field and turbulent flow of flue gas, the trajectory of circulating ash and the pressure loss of the dense flow absorber. The optimal layout form of the baffle plate was determined under the simulated condition. It is found that the chain agitator obviously amplifies the turbulent kinetic energy inside the dense flow absorber, while the increase of revolving speed cannot obviously improve the whole turbulent intensity of flue gas. The double-deck chain agitator can enlarge the area with high turbulent intensity and retard turbulent dissipation. Under this condition, the desired speed of the double-deck chain agitator is 100 r·min-1. Meanwhile, the uniform distribution of flue gas inside the dense flow absorber and the gas-solid sufficient contact can be realized, most of particles are involved in internal recycling, and a small quantity of particles enter the dust catcher. The pressure loss of the system is approximately 200 Pa.
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Key words:
- sintering /
- flue gases /
- desulfurization /
- computer simulation /
- flow fields /
- turbulence /
- particle tracks
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