New synthetic route for the production of mayenite support to enhance Ni resistance to coke deposition in the reforming of tar model compounds

[Display omitted] •Mayenite were synthesized by two innovative routes using different precursors, AlO(OH) + Ca(NO3)2 and Al(OH)3 + Ca(OH)2.•Nickel addition to the carriers was performed via wet impregnation and a one-step method during the mayenite preparation.•The catalyst prepared by one-step meth...

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Bibliographic Details
Published in:Applied catalysis. A, General General, 2019-03, Vol.574, p.48-59
Main Authors: Bracciale, M.P., de Caprariis, B., De Filippis, P., Hernandez, A.D., Scarsella, M.
Format: Article
Language:English
Subjects:
Bayer process
Boehmite
Carbon
Catalysis
Catalyst characterization
Catalysts
Chemical synthesis
Deposition
Gibbsite
Mayenite
Nickel
On-step synthesis
Precursors
Reforming
Selectivity
Slaked lime
Stability analysis
Steam reforming
Tar model compounds
Toluene
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Summary:[Display omitted] •Mayenite were synthesized by two innovative routes using different precursors, AlO(OH) + Ca(NO3)2 and Al(OH)3 + Ca(OH)2.•Nickel addition to the carriers was performed via wet impregnation and a one-step method during the mayenite preparation.•The catalyst prepared by one-step method with boehmite as precursor showed higher tolerance to deactivation by coke.•Different nickel-support interactions due to the applied nickel addition method were verified by TPR analysis. Four nickel/mayenite catalysts were synthesized. Mayenite was prepared from different precursors, namely boehmite (AlO(OH)) + Ca(NO3)2·4H2O and gibbsite + Ca(OH)2, for each couple a specific procedure was followed. The effect of the Ni addition method was also evaluated, comparing wet impregnation and direct inclusion of nickel precursor during mayenite preparation. The obtained catalysts were characterized by XRD, BET, SEM/EDS and TPR. The Ni/mayenite catalysts were tested in steam reforming of toluene and pyrocatechol, chosen as tar model compounds. The experiments were conducted in a fixed-bed lab-scale atmospheric reactor, evaluating carbon conversion, hydrogen selectivity and stability. Characterization of the spent catalysts after toluene steam reforming experiments by XRD and DTG-TPO were performed to assess structural changes and carbon deposition. Kinetic parameters of toluene steam reforming were determined for the different catalysts.
ISSN:0926-860X
1873-3875
DOI:10.1016/j.apcata.2019.01.029