工业安全与环保
工業安全與環保
공업안전여배보
Industrial Safety and Environmental Protection
2015年
9期
13-16
,共4页
柳龙%王浩%杨秀林%秦林波%韩军
柳龍%王浩%楊秀林%秦林波%韓軍
류룡%왕호%양수림%진림파%한군
烧结烟气%NID%脱硫
燒結煙氣%NID%脫硫
소결연기%NID%탈류
sintering flue gas%NID%desulphurization
对烧结烟气NID脱硫工艺入口SO2质量浓度大于2000 mg/m3的情况进行了实验研究。研究结果表明,入口SO2质量浓度为2800 mg/m3条件下,随反应温度升高脱硫效率先升高,在120℃时脱硫效率达到91%,而后趋于平稳;随Ca/S提高,脱硫效率也提高,Ca/S为1.6时,脱硫效率达到91%;H2 O/CaO增大,脱硫效率先上升,在1.8时脱硫效率达到最高91%,而后下降;循环倍率对脱硫效率提升效果显著,在循环倍率150时脱硫效率达到了93.4%。实验结果与现场监测数据表明,较低的烟气入口浓度更利于SO2脱除,高浓度和低浓度SO2工况下的最优操作参数不完全相同。
對燒結煙氣NID脫硫工藝入口SO2質量濃度大于2000 mg/m3的情況進行瞭實驗研究。研究結果錶明,入口SO2質量濃度為2800 mg/m3條件下,隨反應溫度升高脫硫效率先升高,在120℃時脫硫效率達到91%,而後趨于平穩;隨Ca/S提高,脫硫效率也提高,Ca/S為1.6時,脫硫效率達到91%;H2 O/CaO增大,脫硫效率先上升,在1.8時脫硫效率達到最高91%,而後下降;循環倍率對脫硫效率提升效果顯著,在循環倍率150時脫硫效率達到瞭93.4%。實驗結果與現場鑑測數據錶明,較低的煙氣入口濃度更利于SO2脫除,高濃度和低濃度SO2工況下的最優操作參數不完全相同。
대소결연기NID탈류공예입구SO2질량농도대우2000 mg/m3적정황진행료실험연구。연구결과표명,입구SO2질량농도위2800 mg/m3조건하,수반응온도승고탈류효솔선승고,재120℃시탈류효솔체도91%,이후추우평은;수Ca/S제고,탈류효솔야제고,Ca/S위1.6시,탈류효솔체도91%;H2 O/CaO증대,탈류효솔선상승,재1.8시탈류효솔체도최고91%,이후하강;순배배솔대탈류효솔제승효과현저,재순배배솔150시탈류효솔체도료93.4%。실험결과여현장감측수거표명,교저적연기입구농도경리우SO2탈제,고농도화저농도SO2공황하적최우조작삼수불완전상동。
In this paper ,the desulphurization from sintering flue gas by a novel integrated desulfurization system under SO2 initial concentrations above 2 000 mg/m3 is experimentally investigated .The results show that ,with the increase of the reac-tion temperature ,desulphurization efficiency increases firstly ,when the temperature rises at 120 ℃ ,the desulfurization effi-ciency reaches about 91% and then tends to be stable;with the increase of Ca/S ,the desulphurization efficiency also in-creases and when Ca/S is 1 .6 ,the desulphurization efficiency will reach 91% ;with the increase of H2O/CaO ,the desulfu-rization efficiency initially increases ,rising to the highest 91% when it is 1 .8 and then decreases .The circulation ratio sig-nificantly affects the desulphurization efficiency and the desulfurization efficiency can reach 93 .4% when the circulation ratio is 150 .The semi-pilot and field experimental results indicate that lower initial SO2 concentration is more effective to the re-moval of SO2 and there is difference in the optimum operation parameters between a high SO2 initial concentration and a low SO2 concentration .