4.7 Article

Understanding relationship of sepiolite structure tailoring and the catalytic behaviors in glycerol steam reforming over Co/sepiolite derived Co-phyllosilicate catalyst

Journal

RENEWABLE ENERGY
Volume 183, Issue -, Pages 304-320

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.renene.2021.10.097

Keywords

Glycerol steam reforming; Co/sepiolite; Co-phyllosilicate; DFT analysis; Hydrogen production

Funding

  1. National Natural Science Foundation of China [51876001, 51906001]
  2. Key Research and Development Project of Anhui Province [202004a06020053]
  3. University Natural Science Research Project of Anhui Province [KJ2020ZD31]

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Treatment with molten NaOH can enhance the surface area of SEP and improve its surface reactivity, leading to better catalytic performance in bio-glycerol steam reforming.
Bio-glycerol Steam reforming over green and economical Co/sepiolite (SEP) catalysts was a promising strategy to hydrogen production. The activation pretreatment of SEP played a vital role for boosting catalytic behavior of Co/SEP. This work originally explored a full activation of SEP by molten NaOH for tailoring the physicochemical properties of Co-based catalysts prepared by urea precipitation method. Differing from the acid pickling/calcination and molten NaNO3 activation, the molten NaOH treatment enhanced surface area of SEP by desilicication/dealumination effect and further improved the exposure of framework Si and its surface 'reactivity'. According to the characterization results of N-2 adsorption-desorption, XRD, TEM, H-2-TPR, CO/CO2-TPD and XPS, it was found that the feathered Co-phyllosilicate formed on Co/SEP-NaOH catalyst, which enhanced the metal-support interaction, surface area and basic/metallic sites. In contrast, the molten NaNO3 treatment facilitated the transformation of SEP into loughlinite and it was adverse to metal dispersion. Therefore, Co/SEP-NaOH catalyst possessed the highest conversion (92%) and H-2 yield (68%) during the activity test at 600 degrees C and the superior resistance to amorphous coke. Additionally, DFT analysis was introduced to simulate the process of glycerol adsorption and decomposition and demonstrated the Co-CoO interface as the primary reaction sites for the catalytic process. (C) 2021 Elsevier Ltd. All rights reserved.

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