4.5 Article

Glycerol steam reforming over hydrothermal synthetic Ni-Ca/attapulgite for green hydrogen generation

Journal

CHINESE JOURNAL OF CHEMICAL ENGINEERING
Volume 48, Issue -, Pages 176-190

Publisher

CHEMICAL INDUSTRY PRESS CO LTD
DOI: 10.1016/j.cjche.2021.11.004

Keywords

Hydrogen production; Catalysis; Renewable energy; Steam reforming of glycerol; Attapulgite; Nickel catalyst

Funding

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

Ask authors/readers for more resources

In this study, the efficient conversion and utilization of glycerol steam reforming were achieved by optimizing the catalyst structure and preparation method. The appropriate Ca additive and hydrothermal synthesis method improved the catalyst reducibility and CO2 adsorption capacity. The Ni-6Ca/ATP-hs catalyst exhibited the highest glycerol conversion and H-2 yield, as well as excellent anti-sintering and coke resistance.
Glycerol steam reforming (GSR) is one of the promising technologies that can realize renewable hydrogen production and efficient utilization of crude glycerol. To illuminate the functions of Ca content (3%, 6%, 9%, and 12%, by mass) and preparation method for Ni/ATP catalyst structure and its catalytic behaviors, the Ni-xCa/ATP (x = 3%, 6%, 9%, and 12%, by mass) catalysts are prepared by co-impregnation (ci) and hydrothermal synthesis (hs) method and then tested in GSR. Characterization results of XRD, N-2 adsorption-desorption, H-2-TPR, HRTEM, XPS, and NH3/CO2-TPD demonstrate that the combined effect between appropriate Ca additive (6%, by mass) and hs enhance catalyst reducibility, uniform distribution of Ca additive and nickel species over ATP, and adsorption for CO2. This attributes to hs method protects the ATP framework through suppressing the interaction of Ca with ATP and promotes the formation of NiCaOx interface sites. Therefore, Ni-6Ca/ATP-hs exhibits the highest conversion (86.77%) of glycerol to gas product and H-2 yield (76.17%) and selectivity (58.56%) during GSR. Furthermore, XRD, HRTEM, TG-DTG and Raman analyses confirm that Ni-6Ca/ATP-hs also reveals outstanding anti-sintering and coke resistance. In addition, the structural evolution process of Ni/ATP catalyst with Ca introduction and hs method is presented. Considering the high performance, simple preparation process and low cost, the as-prepared catalyst providing new opportunities for utilization of glycerol derived from biodiesel industry. (C) 2021 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.

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