2019
DOI: 10.1038/s41467-019-13560-0
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Near 100% CO selectivity in nanoscaled iron-based oxygen carriers for chemical looping methane partial oxidation

Abstract: Chemical looping methane partial oxidation provides an energy and cost effective route for methane utilization. However, there is considerable CO2 co-production in current chemical looping systems, rendering a decreased productivity in value-added fuels or chemicals. In this work, we demonstrate that the co-production of CO2 can be dramatically suppressed in methane partial oxidation reactions using iron oxide nanoparticles embedded in mesoporous silica matrix. We experimentally obtain near 100% CO selectivity… Show more

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Cited by 124 publications
(80 citation statements)
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“…DFT calculations demonstrated that such a high CO selectivity of confined Fe species in garnet originated from enhanced oxygen vacancy formation energy (Eov) compared with Fe 2 O 3 , which resulted from the lattice oxygen shared by not only reducible Fe ions but also nonreducible Al and Y ones in a garnet structure [25] . Near 100 % CO selectivity was also achieved with higher conversion (Figure 4(a and b)) when decreasing the size of Fe 2 O 3 particles to nanoscale by embedding it into SBA‐15 mesoporous silica which was quite distinct with the previous work involving microscale Fe‐based OCs (Figure 4(c)) [26] . Such the superior selectivity was attributed to smaller average coordination number of surface Fe atoms in nano‐Fe 2 O 3 significantly favoring CH 4 adsorption and low‐coordinated lattice oxygen atoms on the surface of nanoparticle promoting Fe−O bond cleavage as well as CO formation, supported by DFT calculations (Figure 4(d and e)).…”
Section: Oxygen Carriersmentioning
confidence: 53%
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“…DFT calculations demonstrated that such a high CO selectivity of confined Fe species in garnet originated from enhanced oxygen vacancy formation energy (Eov) compared with Fe 2 O 3 , which resulted from the lattice oxygen shared by not only reducible Fe ions but also nonreducible Al and Y ones in a garnet structure [25] . Near 100 % CO selectivity was also achieved with higher conversion (Figure 4(a and b)) when decreasing the size of Fe 2 O 3 particles to nanoscale by embedding it into SBA‐15 mesoporous silica which was quite distinct with the previous work involving microscale Fe‐based OCs (Figure 4(c)) [26] . Such the superior selectivity was attributed to smaller average coordination number of surface Fe atoms in nano‐Fe 2 O 3 significantly favoring CH 4 adsorption and low‐coordinated lattice oxygen atoms on the surface of nanoparticle promoting Fe−O bond cleavage as well as CO formation, supported by DFT calculations (Figure 4(d and e)).…”
Section: Oxygen Carriersmentioning
confidence: 53%
“…Fe 2 O 3 @SBA‐15 oxygen carrier; (d) Calculated energies of CH 4 adsorption. E ad (kJ mol −1 ), on Fe atop site and O atop site of (Fe 2 O 3 ) n nanoparticles as a function of n. The adsorption trends are shown by the blue and red lines; (e) Energy profile of CH 4 partial oxidation on Fe 40 O 60 nanoparticle and Fe 2 O 3 (001) surface [26] . Reproduced with permission from Ref.…”
Section: Oxygen Carriersmentioning
confidence: 99%
“…Chemical looping processes are a promising route for improving energy efficiency, [1][2][3][4] leveraging renewable energy sources, [5][6][7][8][9][10][11] facilitating chemical conversions, [12][13][14][15][16][17][18][19][20] and reducing undesirable emissions across many sectors of the chemical industry. [21][22][23][24][25][26] In a chemical looping (CL) process, the overall reaction is separated into multiple (typically two) subreactions, each mediated by the redox chemistry of a "looped" active material.…”
Section: Introductionmentioning
confidence: 99%
“…Oxidants like O2, H2O and air have been widely used for regenerating OCs 16,17 , and thus the CLCS process lowers the requirement for extra purification and exhibits the potential of directly utilizing impure CO2. Different from well-known dry reforming of CO2 18,19 , the CLCS process takes advantage of producing syngas with controllable H2/CO ratio and pure CO 15,20 . In addition, the separately obtained syngas and CO products can be directly used for green acetic acid production 15 .…”
Section: Introductionmentioning
confidence: 99%