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Study of catalytic hydrodeoxygenation performance of Ni catalysts: Effects of prepared method

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  • Chen, Shuang
  • Miao, Caixia
  • Luo, Yan
  • Zhou, Guilin
  • Xiong, Kun
  • Jiao, Zhaojie
  • Zhang, Xianming

Abstract

Ni-HT, Ni-ST, Ni-PC, and Ni-CA catalysts were synthesized using hard-template, soft-template, co-precipitation, and complex methods, respectively, characterized by XRD, BET, H2-TPR, and H2-TPD technology. The catalytic hydrodeoxygenation performance of the prepared Ni catalysts was evaluated by using ethyl acetate as the model compound. The prepared Ni catalyst activities are in the following order: Ni-HT > Ni-ST > Ni-PC > Ni-CA. Ni-HT and Ni-ST catalysts have developed pore structure; they show large specific surface area of 90.2 and 45.4 m2/g, respectively. The active phase of the catalyst is well dispersed, the active sites are widely distributed, thereby promoting the effective activation for reactant molecules. Ethyl acetate can be completely converted over Ni-HT and Ni-ST catalysts at 300 °C and 320 °C, respectively, and the ethane selectivity reaches 97.8% and 97.2%. Ni-PC and Ni-CA catalysts are mainly composed of dense particles, and have low specific surface areas of 11.2 and 2.4 m2/g, respectively. The crystallinity of the active phase is poor, the activation ability for the hydrogen molecule is obviously weaker than that of Ni-HT and Ni-ST catalysts. Ethyl acetate can be completely converted with the activity of Ni-PC and Ni-CA catalysts at 360 °C and 380 °C, and the ethane selectivity reached 96.7% and 93.5%, respectively.

Suggested Citation

  • Chen, Shuang & Miao, Caixia & Luo, Yan & Zhou, Guilin & Xiong, Kun & Jiao, Zhaojie & Zhang, Xianming, 2018. "Study of catalytic hydrodeoxygenation performance of Ni catalysts: Effects of prepared method," Renewable Energy, Elsevier, vol. 115(C), pages 1109-1117.
    • Handle: RePEc:eee:renene:v:115:y:2018:i:c:p:1109-1117
    DOI: 10.1016/j.renene.2017.09.028
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    References listed on IDEAS

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    1. Jack P. C. Kleijnen, 2015. "Response Surface Methodology," International Series in Operations Research & Management Science, in: Michael C Fu (ed.), Handbook of Simulation Optimization, edition 127, chapter 0, pages 81-104, Springer.
    2. Ma, Yingqun & Wang, Qunhui & Sun, Xiaohong & Wu, Chuanfu & Gao, Zhen, 2017. "Kinetics studies of biodiesel production from waste cooking oil using FeCl3-modified resin as heterogeneous catalyst," Renewable Energy, Elsevier, vol. 107(C), pages 522-530.
    3. Arun, Naveenji & Sharma, Rajesh V. & Dalai, Ajay K., 2015. "Green diesel synthesis by hydrodeoxygenation of bio-based feedstocks: Strategies for catalyst design and development," Renewable and Sustainable Energy Reviews, Elsevier, vol. 48(C), pages 240-255.
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    Cited by:

    1. Lv, Wei & Hu, Xiaohong & Zhu, Yuting & Xu, Ying & Liu, Shijun & Chen, Peili & Wang, Chenguang & Ma, Longlong, 2022. "Molybdenum oxide decorated Ru catalyst for enhancement of lignin oil hydrodeoxygenation to hydrocarbons," Renewable Energy, Elsevier, vol. 188(C), pages 195-210.
    2. Miao, Caixia & Zhou, Guilin & Chen, Shuang & Xie, Hongmei & Zhang, Xianming, 2020. "Synergistic effects between Cu and Ni species in NiCu/γ-Al2O3 catalysts for hydrodeoxygenation of methyl laurate," Renewable Energy, Elsevier, vol. 153(C), pages 1439-1454.
    3. Chen, Shuang & Zhou, Guilin & Miao, Caixia, 2019. "Green and renewable bio-diesel produce from oil hydrodeoxygenation: Strategies for catalyst development and mechanism," Renewable and Sustainable Energy Reviews, Elsevier, vol. 101(C), pages 568-589.
    4. Li, Xiangping & Chen, Lei & Chen, Guanyi & Zhang, Jianguang & Liu, Juping, 2020. "The relationship between acidity, dispersion of nickel, and performance of Ni/Al-SBA-15 catalyst on eugenol hydrodeoxygenation," Renewable Energy, Elsevier, vol. 149(C), pages 609-616.

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