Journal
FUEL PROCESSING TECHNOLOGY
Volume 206, Issue -, Pages -Publisher
ELSEVIER
DOI: 10.1016/j.fuproc.2020.106467
Keywords
Coal liquefaction residue; Activated carbon; KOH activation; Sulfur-rich sorbent; Elemental mercury removal
Funding
- Foundation of CHN ENERGY 2030 Project [GJNY2030XDXM-19-17]
- Innovative Project for Postgraduate Education of Shanxi Province [2019SY181]
- National Natural Science Foundation of China [U1710107]
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Recent, carbon-based adsorption technology, especially activated carbon with element-doping treatment, has been considered an effective approach to capture elemental mercury (Hg-0) from coal-fired flue gas. In this study, a novel sulfur-rich activated carbon (S/AC) was in-situ derived from coal liquefaction residue (CLR) with KOH activation, which can make full use of the sulfur in CLR and simplify the preparation process. The effects of KOH to CLR weight ratios and activation temperatures on Hg-0 removal performance were discussed. The S/AC was characterized by N-2 adsorption/desorption, XRD, SEM, TEM-EDS, XPS and Hg-TPD techniques. A fixed-bed reactor was used to estimate the Hg-0 removal performance of sorbents. The effects of adsorption temperatures and flue gas components on Hg-0 removal performance were also evaluated. The sorbent exhibited excellent Hg-0 removal performance with the KOH to CLR weight ratio of 1:2 and the activation temperature of 800 degrees C. The Hg-0 removal efficiency was stabilized at 97% at 60-120 degrees C with a gas hourly space velocity (GHSV) of 7.5 x 10(4) h(-1). Both SO2 and NO exhibited positive influences on S/AC sorbents for Hg-0 capture. The XPS and Hg-TPD results indicated that sulfur is primary active site for Hg-0 removal, and the mercury adsorbed on S/AC sorbent was HgS. The research indicated that CLR is a potential raw material for synthesizing high efficient S/AC sorbents for Hg-0 removal from flue gas.
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