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Tri-reforming of methane over Ni/ZrO2 catalyst derived from Zr-MOF for the production of synthesis gas
The increasing concentration of CO 2 and CH 4 in the environment is a global concern. Tri-reforming of methane (TRM) is a promising route for the conversion of these two greenhouse gases to more valuable synthesis gas with an H 2 /CO ratio of 1.5–2. In this study, a series of Zr-MOF synthesized via...
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Published in: | Environmental science and pollution research international 2024-05, Vol.31 (24), p.35069-35082 |
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Main Authors: | , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites |
Online Access: | Get full text |
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Summary: | The increasing concentration of CO
2
and CH
4
in the environment is a global concern. Tri-reforming of methane (TRM) is a promising route for the conversion of these two greenhouse gases to more valuable synthesis gas with an H
2
/CO ratio of 1.5–2. In this study, a series of Zr-MOF synthesized via the solvothermal method and impregnation technique was used to synthesize the nickel impregnated on MOF-derived ZrO
2
catalyst. The catalyst was characterized by various methods, including N
2
-porosimetry, X-ray diffraction (XRD), temperature programmed reduction (TPR), CO
2
-temperature programmed desorption (CO
2
-TPD), thermo-gravimetric analysis (TGA), chemisorption, field-emission scanning electron microscopy (FE-SEM), and high-resolution transmission electron microscopy (HR-TEM). Characterization results confirmed the formation of the Zr-MOF and nickel metal dispersed on MOF-derived ZrO
2
. Further, the tri-reforming activity of the catalyst developed was evaluated in a downflow-packed bed reactor. The various catalysts were screened for TRM activity at different temperatures (600–850 °C). Results demonstrated that TRM was highly favorable over the NZ-1000 catalyst due to its desirable physicochemical properties, including nickel metal surface area (2.3 m
2
/g
cat
−1
), metal dispersion (7.1%), and nickel metal reducibility (45%), respectively. Over the NZ-1000 catalyst, an optimum H
2
/CO ratio of ~ 1.6–2 was achieved at 750 °C, and it was stable for a longer period of time.
Graphical Abstract |
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ISSN: | 1614-7499 0944-1344 1614-7499 |
DOI: | 10.1007/s11356-024-33549-7 |