2020
DOI: 10.1016/j.fuel.2020.117105
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Regenerable CoxMn3−xO4 spinel sorbents for elemental mercury removal from syngas: Experimental and DFT studies

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Cited by 33 publications
(23 citation statements)
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“…As shown in Figure 2, the XRD pattern of the prepared single manganese oxide in the presence of VC (Mn 2 O 3 − 0.3VC, Figure 2a) revealed characteristic Mn 2 O 3 diffractions 44,48 Especially, on increasing the calcination temperature to 500 °C, the crystallinity of the Mn 3 Co 2 O x − 0.3VC-500 catalyst (Figure 2c) was significantly enhanced and obvious diffraction peaks belonging to the Mn−Co spinel structure (JCPDS#18-0408) could be observed. The Mn−Co oxides prepared with different VC contents (Figure 2d, 0− 0.4VC) revealed a similar crystalline structure to that of the Mn 3 Co 2 O x −0.3VC catalyst.…”
Section: Resultsmentioning
confidence: 97%
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“…As shown in Figure 2, the XRD pattern of the prepared single manganese oxide in the presence of VC (Mn 2 O 3 − 0.3VC, Figure 2a) revealed characteristic Mn 2 O 3 diffractions 44,48 Especially, on increasing the calcination temperature to 500 °C, the crystallinity of the Mn 3 Co 2 O x − 0.3VC-500 catalyst (Figure 2c) was significantly enhanced and obvious diffraction peaks belonging to the Mn−Co spinel structure (JCPDS#18-0408) could be observed. The Mn−Co oxides prepared with different VC contents (Figure 2d, 0− 0.4VC) revealed a similar crystalline structure to that of the Mn 3 Co 2 O x −0.3VC catalyst.…”
Section: Resultsmentioning
confidence: 97%
“…According to the X-ray diffraction (XRD) results and previous works (Figure ), a Mn–Co tetragonal crystal structure (Mn 2 CoO 4 , mp-1221996) was selected from the Materials Project as the calculation model to simulate the Mn–Co spinel oxides in this study. To ensure the rationality of the calculation results, the XRD pattern of the selected model was calculated. It has been found that the simulated XRD pattern of the Mn–Co model was well consistent with the Mn 3 Co 2 O x –0.3VC-500 catalyst (Figure S1), demonstrating that the calculations are faithworthy.…”
Section: Methodsmentioning
confidence: 99%
“…The excellent catalytic activity of copper-manganese oxide is closely related to the flexible valence states of Cu +/2+ and Mn 2+/3+/4+ [33]. The valence state changes of copper and manganese cations easily lead to an electron-transfer environment [34], which is beneficial to the adsorption and oxidation of Hg 0 . Therefore, our previous work synthesized copper-manganese spinel-type oxide and used to remove Hg 0 from simulated flue gas (4% O 2 + 12% CO 2 + N 2 ) [35][36][37].…”
Section: Introductionmentioning
confidence: 99%
“…34 As shown in Figure 2, Hg 0 adsorbent injection is an effective technology for Hg 0 removal. 40,41 Hg 0 adsorbent is usually injected between the downstream of the air preheater (APH) and the upstream of particulate control device such as ESP or FF. 42 Among various Hg 0 adsorbents, activated carbon is one of the most universal Hg 0 adsorbents.…”
Section: Introductionmentioning
confidence: 99%
“…As shown in Figure , Hg 0 adsorbent injection is an effective technology for Hg 0 removal. , Hg 0 adsorbent is usually injected between the downstream of the air preheater (APH) and the upstream of particulate control device such as ESP or FF . Among various Hg 0 adsorbents, activated carbon is one of the most universal Hg 0 adsorbents. However, as activated carbon has the disadvantage of high cost, it is necessary to find other moderate adsorbents which can replace activated carbon for Hg 0 removal effectively and economically. Among other moderate Hg 0 adsorbents, fly ash obtained from coal-fired power plant (CFPP) can be used as a promising substitute for activated carbon for Hg 0 removal with the advantages of low cost, abundance, and easy access .…”
Section: Introductionmentioning
confidence: 99%