2021
DOI: 10.9767/bcrec.17.1.12501.88-102
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The Ni Catalyst Supported on the FSP-made Transition Metal (Co, Mn, Cu or Zn) Doped La2O3 Material for the Dry Reforming of Methane

Abstract: The transition metal (Co, Mn, Cu or Zn) doped La2O3 material was prepared by flame spray pyrolysis (FSP) technique. The 2 wt.% Ni catalyst supported on this material was characterized by XRD, N2 physisorption, TPR, H2 chemisorption and TGA, and evaluated by the dry reforming of methane (DRM). The perovskite structure was certainly formed when either Co or Mn was introduced. The Cu can generate the La2CuO4 spinel phase while the Zn showed a mixed phase of La2O3, ZnO and La(OH)3. The Ni/Co-La2O3 catalyst was mor… Show more

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Cited by 4 publications
(2 citation statements)
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“…As for CoMnZn/SiO 2 , the reduction peak at 265 °C was assigned to the partial reduction of Co 2 ZnO 4 and Co 2 MnO 4 composite oxides, and the latter peak at about 420 °C was further reduced to metallic Co (Co δ+ to Co 0 ). 14,18,55 Compared with CoMnZn/SiO 2 , the reduction temperature corresponded to the second reduction step for CoMnZn/Al 2 O 3 , increasing from 420 to 480 °C, while the first peak shifted from 265 to 250 °C. However, for TiO 2 -supported catalysts, both reduction peaks shifted toward a lower temperature, where the first peak shifted to 240 °C and the second peak shifted to 390 °C (CoMnZn/r-TiO 2 ), 400 °C (CoMnZn/P25), and 415 °C (CoMnZn/a-TiO 2 ), respectively.…”
Section: Co Conversion (Co Co )/Co 100%mentioning
confidence: 99%
“…As for CoMnZn/SiO 2 , the reduction peak at 265 °C was assigned to the partial reduction of Co 2 ZnO 4 and Co 2 MnO 4 composite oxides, and the latter peak at about 420 °C was further reduced to metallic Co (Co δ+ to Co 0 ). 14,18,55 Compared with CoMnZn/SiO 2 , the reduction temperature corresponded to the second reduction step for CoMnZn/Al 2 O 3 , increasing from 420 to 480 °C, while the first peak shifted from 265 to 250 °C. However, for TiO 2 -supported catalysts, both reduction peaks shifted toward a lower temperature, where the first peak shifted to 240 °C and the second peak shifted to 390 °C (CoMnZn/r-TiO 2 ), 400 °C (CoMnZn/P25), and 415 °C (CoMnZn/a-TiO 2 ), respectively.…”
Section: Co Conversion (Co Co )/Co 100%mentioning
confidence: 99%
“…Nickel-based catalysts have been extensively available for an enormous variety of high-temperature thermo-catalytic applications, such as hydrocarbon reforming and methanation reactions. The major challenge for nickel-based catalysts is rooted in the potential deactivation by metal sintering and carbon deposition during high-temperature reactions . The CH 4 decomposition (eq ) and CO disproportionation (eq ) reactions are the main reasons for coking on nickel-based catalysts.…”
Section: Progress On Spinel Catalysts For Thermal-driven C1 Conversionmentioning
confidence: 99%