4.7 Article

Simultaneous removal of NO and elemental mercury from coal-fired flue gas using natural ferruginous manganese ore at low temperature

Journal

FUEL
Volume 326, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2022.125118

Keywords

Nitric oxide; Elemental mercury; Flue gas; Ferruginous manganese ore; Simultaneous removal

Funding

  1. National Natural Science Foundation of China [52106168, 51776084]
  2. Natural Science Foundation of Shandong Province [ZR2020QE202]
  3. Guangdong Basic and Applied Basic Research Foundation [2020A1515111197]
  4. China Postdoctoral Science Foundation [2020M682179]
  5. Youth Innovation Program of Universities in Shandong Province [2019KJD007]

Ask authors/readers for more resources

Natural ferruginous manganese ore (FMO) was developed as an economical NH3-SCR catalyst for simultaneous elimination of NO and elemental mercury (Hg0) from coal-fired flue gas. The chemical composition, pore structure, crystal structure and surface chemistry of FMO were characterized and the effects of various parameters on the removal efficiency of NO and Hg0 were studied. The results showed that FMO exhibited high removal efficiency for both NO and Hg0 under optimal conditions.
Natural ferruginous manganese ore (FMO) was developed as a cost-effective NH3-SCR catalyst for the simultaneous removal of NO and elemental mercury (Hg0) from coal-fired flue gas. The chemical composition, pore structure, crystal structure and surface chemistry of FMO were characterized by different methods. The results showed that FMO was constructed with sheet-like structures. There were massive slit-shaped pores in the FMO. Manganese and iron oxides existed in an amorphous form. After calcination, the NO removal performance of FMO was obviously decreased due to the decomposition of MnO2. A high NH3/NO ratio was conductive to NO removal but excessive NH3 was unnecessary for NO removal. NO could promote Hg0 removal whereas Hg0 had little effect on NO removal. The effects of different SCR atmosphere (inlet, middle layer, and outlet), reaction temperature (100 degrees C-400 degrees C), and flue gas composition (O2 and SO2) on NO/Hg0 removal was also studied. At the optimal temperature (200 degrees C), the NO removal efficiency was greater than 80% and the Hg0 removal efficiency was close to 100%. To some extent, FMO presented preferable SO2 poisoning resistance probably because of the presence of iron oxide. The mechanism of NO/Hg0 removal over FMO was further described. Both fast SCR and conventional SCR reactions happened over FMO during NO removal. Mn4+, Fe3+, and lattice oxygen were first consumed and then replenished by gaseous O2. FMO served as a catalyst for Hg0 oxidation during a long period of denitration process.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available