HCl removal characteristics of calcium hydroxide at the dry-type sorbent reaction accelerator using municipal waste incinerator flue gas at a real site

被引:23
|
作者
Kim, Kwang-Deuk [1 ,2 ]
Jeon, Seong-Min [1 ,2 ]
Hasolli, Naim [1 ,2 ]
Lee, Kang-San [1 ,2 ]
Lee, Jae-Rang [1 ,2 ]
Han, Jae-Won [3 ]
Kim, Hee Taik [3 ]
Park, Young-Ok [1 ,2 ]
机构
[1] Korea Inst Energy Res, Solar Thermal Lab, Daejeon 34129, South Korea
[2] Korea Inst Energy Res, Clean Fuel Lab, Daejeon 34129, South Korea
[3] Hanyang Univ, Dept Fus Chem Engn, Ansan 15588, South Korea
关键词
Sorbent Reaction Accelerator (SRx); Stoichiometric Ratio; HCl; Ca(OH)(2); Baghouse; ACTIVATED CARBON; KINETICS; SO2;
D O I
10.1007/s11814-016-0306-0
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A dry-type reactor was used to reduce the HCl emitted from a municipal waste incinerator. A real-scale reactor was installed downstream of the existing semi-dry reactor (SDR) as part of D local incineration plant, whose HCl removal efficiency was investigated by applying calcium hydroxide (Ca(OH)(2)). A test dry-type sorbent reaction accelerator (SRx) was designed, and the stoichiometric ratio (SR) of the sorbent and the secondary reaction characteristics of unreacted Ca(OH)(2) in a baghouse were analyzed. For the results, the SRx showed higher HCl removal efficiency and more economic benefits than the other existing flue gas treatment facilities of the incinerator plant. Furthermore, the highest reduction efficiency of HCl was obtained when the differential pressure in the baghouse was maintained at 150mmH(2)O. This is because as the unreacted sorbent attached to the filter surface layer became thicker and the secondary reaction of the HCl removal increased.
引用
收藏
页码:747 / 756
页数:10
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  • [1] HCl removal characteristics of calcium hydroxide at the dry-type sorbent reaction accelerator using municipal waste incinerator flue gas at a real site
    Kwang-Deuk Kim
    Seong-Min Jeon
    Naim Hasolli
    Kang-San Lee
    Jae-Rang Lee
    Jae-Won Han
    Hee Taik Kim
    Young-Ok Park
    Korean Journal of Chemical Engineering, 2017, 34 : 747 - 756