Jin Dong-Seop, Deshwal Bal-Raj, Park Young-Seong, Lee Hyung-Keun
Flue Gas Treatment Center, Korea Institute of Energy Research, Daejon 305 600, Republic of Korea.
J Hazard Mater. 2006 Jul 31;135(1-3):412-7. doi: 10.1016/j.jhazmat.2005.12.001. Epub 2006 Jan 25.
The present study attempts to generate chlorine dioxide (ClO(2)) gas continuously by chlorate-chloride process and to utilize it further to clean up SO(2) and NO(x) gases simultaneously from the flue gas in the lab-scale bubbling reactor. Experiments were carried out to examine the effect of various operating parameters like input SO(2) concentration, input NO concentration, pH of the reaction medium, and ClO(2) feeding rate on the SO(2) and NO(x) removal efficiencies at 45 degrees C. Complete oxidation of NO into NO(2) occurred on passing sufficient ClO(2) gas into the scrubbing solution. SO(2) removal efficiency of about 100% and NO(x) removal efficiency of 66-72% were achieved under optimized conditions. NO(x) removal efficiency decreased slightly with increasing pH and NO concentration. Input SO(2) concentration had marginal catalytic effect on NO(2) absorption. No improvement in the NO(x) removal efficiency was observed on passing excess of chlorine dioxide in the scrubbing solution.
本研究试图通过氯酸盐-氯化物工艺连续生成二氧化氯(ClO₂)气体,并在实验室规模的鼓泡反应器中进一步利用它同时净化烟道气中的SO₂和NOₓ气体。进行了实验,以考察诸如输入SO₂浓度、输入NO浓度、反应介质的pH值以及ClO₂进料速率等各种操作参数对45℃下SO₂和NOₓ去除效率的影响。向洗涤溶液中通入足够的ClO₂气体时,NO完全氧化为NO₂。在优化条件下,SO₂去除效率约为100%,NOₓ去除效率为66-72%。NOₓ去除效率随pH值和NO浓度的增加而略有下降。输入SO₂浓度对NO₂吸收有轻微的催化作用。在洗涤溶液中通入过量二氧化氯时,未观察到NOₓ去除效率的提高。