Abstract
Mercury pollution is created by coal combustion processes in multi-component systems. Adsorbent injection was identified as a potential strategy for capturing Hg0 from waste gases, with adsorbents serving as the primary component. The hydrothermal approach was used to synthesize a series of MnOx–CeOx nanorod adsorbents with varying Mn/Ce molar ratios to maximize the Hg0 capture capabilities. Virgin CeOx had weak Hg0 elimination activity; <8% Hg0 removal efficiency was obtained from 150 °C to 250 °C. With the addition of MnOx, the amount of surface acid sites and the relative concentration of Mn4+ increased. This ensured the sufficient adsorption and oxidation of Hg0 while overcoming the limitations of restricted adsorbate-adsorbent interactions caused by the lower surface area, endowing MnOx–CeOx with increased Hg0 removal capacity. When the molar ratio of Mn/Ce reached 6/4, the adsorbent’s Hg0 removal efficiency remained over 92% at 150 °C and 200 °C. As the molar ratio of Mn/Ce grew, the adsorbent’s Hg0 elimination capacity declined due to decreased surface area, weakened acidity, and decreased activity of Mn4+; <75% Hg0 removal efficiency was reached between 150 °C and 250 °C for virgin MnOx. Throughout the overall Hg0 elimination reactions, Mn4+ and Oα were in charge of oxidizing Hg0 to HgO, with Ce4+ acting as a promoter to aid in the regeneration of Mn4+. Because of its limited adaptability to flue gas components, further optimization of the MnOx–CeOx nanorod adsorbent is required.
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Abbreviations
- M :
-
Usage of the examined sample (g)
- f :
-
Flow rate of the simulated flue gas (mL/min)
- t :
-
Hg0 elimination time (min)
- q t :
-
Capture capacity of Hg0 (μg/g)
- ƞ :
-
Removal efficiency of Hg0 (%)
- X out :
-
Outlet Hg0 concentration (μg/m3)
- X in :
-
Inlet Hg0 concentration (μg/m3)
- B :
-
Potential mass transfer index (mg/g)
- b :
-
Adsorbate–adsorbent affinity parameter (g·h/mg)
- [k L a]f :
-
External mass transfer factor (h−1)
- [k L a]g :
-
Global mass transfer factor (h−1)
- [k L a]d :
-
Internal mass transfer factor (h−1)
- k 1 :
-
Pseudo-first-order rate constant (min−1)
- k 2 :
-
Pseudo-second-order rate constant (min−1)
- q e :
-
Theoretical Hg0 capture capacity (μg/g)
- k p :
-
Intraparticle diffusion coefficient (μg/(g·min1/2))
- c :
-
Constant corresponding to the boundary conditions (μg/g)
- α :
-
Initial adsorption rate constant (μg/(g·min1/2))
- β :
-
Desorption rate constant (g/μg)
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Funding
This work is supported by the Fundamental Research Funds in China Jiliang University, the Zhejiang Provincial Department of Education General Research Project in 2023 (No. Y202353660), and the Zhejiang Provincial Natural Science Foundation of China (No. LQ22E060003).
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SG: investigation, validation, writing—original draft. YH: Investigation. ZJ: Investigation. XW: Validation. YW: Writing—review and editing. HW: Writing—review and editing. DY: Conceptualization, writing—review and editing, supervision.
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Gao, S., Wang, X., Wang, Y. et al. Mechanistic investigation on the Hg0 elimination ability of MnOx–CeOx nanorod adsorbents: effects of Mn/Ce molar ratio. Waste Dispos. Sustain. Energy (2024). https://doi.org/10.1007/s42768-023-00181-z
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DOI: https://doi.org/10.1007/s42768-023-00181-z