Abstract:Environmentally benign zinc sulfide
(ZnS), consisting entirely
of “active” sites, has shown promising efficiency for
capturing mercury from flue gas in recent experimental studies. In
this work, the binding mechanism of Hg0 on the ZnS(110)
surface was investigated by the density functional theory (DFT) method.
Meanwhile, the binding of two additional mercury forms, HgCl and HgCl2, and three essential flue gas components, H2O,
SO2, and HCl, and their further effects on the strength
of Hg0 binding on the ZnS(110… Show more
“…The activation energies of Hg 0 adsorbed on the Cu-terminated sites of CuO and on Zn of ZnS are around 100 kJ/mol. ,, This value is lower than that for mercury sulfides. Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg–Cu amalgam over nano-CuS, like the Hg–Zn amalgam on the ZnS surface . Moreover, this desorption temperature is quite near the desorption temperature of the Hg–Ag amalgam .…”
Section: Resultsmentioning
confidence: 84%
“…Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg−Cu amalgam over nano-CuS, like the Hg−Zn amalgam on the ZnS surface. 61 Moreover, this desorption temperature is quite near the desorption temperature of the Hg−Ag amalgam. 62 To further confirm this point, extensive Hg-TPD testing was conducted over copper powder.…”
Section: ■ Results and Discussionmentioning
confidence: 85%
“…The peak centered at 201 °C was assigned to metacinnabar (β-HgS), and the peak located at 303 °C was due to the decomposition of cinnabar (α-HgS). ,, The decomposition energy for mercury sulfides has been reported to be from 135 to 185 kJ/mol . The activation energies of Hg 0 adsorbed on the Cu-terminated sites of CuO and on Zn of ZnS are around 100 kJ/mol. ,, This value is lower than that for mercury sulfides. Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg–Cu amalgam over nano-CuS, like the Hg–Zn amalgam on the ZnS surface .…”
Nanostructured copper sulfide synthesized with the assistance of surfactant with nanoscale particle size and high Brunauer-Emmett-Teller surface area was for the first time applied for the capture of elemental mercury (Hg) from coal combustion flue gas. The optimal operation temperature of nano-CuS for Hg adsorption is 75 °C, which indicates that injection of the sorbent between the wet flue gas desulfurization and the wet electrostatic precipitator systems is feasible. This assures that the sorbent is free of the adverse influence of nitrogen oxides. Oxygen (O) and sulfur dioxide exerted a slight influence on Hg adsorption over the nano-CuS. Water vapor was shown to moderately suppress Hg capture efficiency via competitive adsorption. The simulated adsorption capacities of nano-CuS for Hg under pure nitrogen (N), N + 4% O, and simulated flue gas reached 122.40, 112.06, and 89.43 mgHg/g nano-CuS, respectively. Compared to those of traditional commercial activated carbons and metal sulfides, the simulated adsorption capacities of Hg over the nano-CuS are at least an order of magnitude higher. Moreover, with only 5 mg loaded in a fixed-bed reactor, the Hg adsorption rate reached 11.93-13.56 μg/g min over nano-CuS. This extremely speedy rate makes nano-CuS promising for a future sorbent injection technique. The anisotropic growth of nano-CuS was confirmed by X-ray diffraction analysis and provided a fundamental aspect for nano-CuS surface reconstruction and polysulfide formation. Further X-ray photoelectron spectroscopy and Hg temperature-programmed desorption tests showed that the active polysulfide, S-S dimers, and copper-terminated sites contributed primarily to the extremely high Hg adsorption capacity and rate. With these advantages, nano-CuS appears to be a highly promising alternative to traditional sorbents for Hg capture from coal combustion flue gas.
“…The activation energies of Hg 0 adsorbed on the Cu-terminated sites of CuO and on Zn of ZnS are around 100 kJ/mol. ,, This value is lower than that for mercury sulfides. Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg–Cu amalgam over nano-CuS, like the Hg–Zn amalgam on the ZnS surface . Moreover, this desorption temperature is quite near the desorption temperature of the Hg–Ag amalgam .…”
Section: Resultsmentioning
confidence: 84%
“…Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg−Cu amalgam over nano-CuS, like the Hg−Zn amalgam on the ZnS surface. 61 Moreover, this desorption temperature is quite near the desorption temperature of the Hg−Ag amalgam. 62 To further confirm this point, extensive Hg-TPD testing was conducted over copper powder.…”
Section: ■ Results and Discussionmentioning
confidence: 85%
“…The peak centered at 201 °C was assigned to metacinnabar (β-HgS), and the peak located at 303 °C was due to the decomposition of cinnabar (α-HgS). ,, The decomposition energy for mercury sulfides has been reported to be from 135 to 185 kJ/mol . The activation energies of Hg 0 adsorbed on the Cu-terminated sites of CuO and on Zn of ZnS are around 100 kJ/mol. ,, This value is lower than that for mercury sulfides. Therefore, it is quite possible that the desorption peak at 120 °C was assigned to Hg–Cu amalgam over nano-CuS, like the Hg–Zn amalgam on the ZnS surface .…”
Nanostructured copper sulfide synthesized with the assistance of surfactant with nanoscale particle size and high Brunauer-Emmett-Teller surface area was for the first time applied for the capture of elemental mercury (Hg) from coal combustion flue gas. The optimal operation temperature of nano-CuS for Hg adsorption is 75 °C, which indicates that injection of the sorbent between the wet flue gas desulfurization and the wet electrostatic precipitator systems is feasible. This assures that the sorbent is free of the adverse influence of nitrogen oxides. Oxygen (O) and sulfur dioxide exerted a slight influence on Hg adsorption over the nano-CuS. Water vapor was shown to moderately suppress Hg capture efficiency via competitive adsorption. The simulated adsorption capacities of nano-CuS for Hg under pure nitrogen (N), N + 4% O, and simulated flue gas reached 122.40, 112.06, and 89.43 mgHg/g nano-CuS, respectively. Compared to those of traditional commercial activated carbons and metal sulfides, the simulated adsorption capacities of Hg over the nano-CuS are at least an order of magnitude higher. Moreover, with only 5 mg loaded in a fixed-bed reactor, the Hg adsorption rate reached 11.93-13.56 μg/g min over nano-CuS. This extremely speedy rate makes nano-CuS promising for a future sorbent injection technique. The anisotropic growth of nano-CuS was confirmed by X-ray diffraction analysis and provided a fundamental aspect for nano-CuS surface reconstruction and polysulfide formation. Further X-ray photoelectron spectroscopy and Hg temperature-programmed desorption tests showed that the active polysulfide, S-S dimers, and copper-terminated sites contributed primarily to the extremely high Hg adsorption capacity and rate. With these advantages, nano-CuS appears to be a highly promising alternative to traditional sorbents for Hg capture from coal combustion flue gas.
In the work, sulfur-containing
sorbents were employed to remove
elemental mercury (Hg0) from coal-fired flue gas. The work
used the thermogravimetric analysis, Brunauer–Emmett–Teller method, scanning electron microscopy with energy-dispersive spectroscopy,
X-ray diffraction, and X-ray photoelectron spectroscopy to characterize
the physicochemical properties of the sorbents. The Hg0 removal performance of these used sorbents from the simulated coal-fired
flue gas was evaluated by a bench-scale fixed-bed reactor. The results
indicated that a generous amount of elemental sulfur covered the surface
and pore structure of the used sorbent. With the rise of H2S selective oxidation temperature, both the sulfur content and specific
surface area decreased rapidly. Used-Fe/SC120 could achieve the mercury removal
efficiency of above 90% at 90 °C. The high temperature was not
conducive to the mercury capture due to the release of surface elemental
sulfur. The presence of O2 and SO2 inhibited
Hg0 removal in different degrees because of the decreased
active sulfur sites and competitive adsorption. Meanwhile, NO promoted
the Hg0 removal efficiency by enhancing the Hg0 oxidation. The further
analysis showed that the surface elemental sulfur was vital to capture
the Hg0 from coal-fired flue gas, which reacted with Hg0 to form HgS.
“…The desorption/decomposition peak in the Hg‐TPD pattern of Hg‐laden 0.8NC‐ZIF centering at 265 °C indexed to the characteristic decomposition temperature of HgSe . Although the Cu‐terminated sites in CuSe probably acted as the adsorption center for Hg 0 capture in metal chalcogenides, the mercury in as‐formed amalgam will be trapped by Se 2− immediately due to the exceedingly high affinity between mercury and Se 2− . This contributes to that the adsorbed mercury exists primarily as HgSe instead of Hg‐Cu amalgam over the 0.8NC‐ZIF surface.…”
A key challenge in elemental mercury (Hg 0 ) decontamination from flue gas lies in the design of a sorbent with abundant reactive adsorption sites that exhibit high affinity toward Hg 0 to simultaneously achieve rapid capture and large capacity. Herein, zeolitic imidazolate framework-8 (ZIF-8) supported copper selenide (CuSe) nanocomposites are synthesized by a newly designed two-step surfactant-assisted method. The as-prepared CuSe/ZIF-8 with CuSe to ZIF-8 mass ratio of 80% (0.8NC-ZIF) exhibits unparalleled performance toward Hg 0 adsorption with equilibrium capacity and average rate reaching 309.8 mg g −1 and 105.3 µg g −1 min −1 , respectively, surpassing all reported metal sulfides and traditional activated-carbon-based sorbents. The impressive performance of 0.8NC-ZIF for Hg 0 immobilization is primarily attributed to the adequate exposure of the Se-terminated sites with high affinity toward Hg 0 resulted from the layered structure of CuSe. The adsorbed mercury selenide exhibits even higher stability than the most stable natural mercury ore-that is, mercury sulfide-hence minimizing its environmental impact when the CuSe/ZIF-8 sorbent is dumped. This work provides a new mindset for future design of sorbents for efficient Hg 0 capture from industrial flue gas. The results also justify the candidature of CuSe/ZIF to be applicable for mercury pollution remediation in real-world conditions.
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