Bio-Oil Steam Reforming over a Mining Residue Functionalized with Ni as Catalyst: Ni-UGSO

被引:8
|
作者
Bali, Amine [1 ]
Blanchard, Jasmin [1 ]
Chamoumi, Mostafa [1 ]
Abatzoglou, Nicolas [1 ]
机构
[1] Univ Sherbrooke, Dept Chem Engn & Biotechnol Engn, 2500 Blvd Univ, Sherbrooke, PQ J1K 2R1, Canada
关键词
bio-oil; catalysis; steam reforming; mining residue; nickel catalyst; spinel; hydrogen; syngas; HYDROGEN-PRODUCTION; FAST PYROLYSIS; THERMODYNAMIC ANALYSIS; PARTIAL OXIDATION; SYNGAS PRODUCTION; MODEL COMPOUNDS; PART; BIOMASS; LIQUID; COMPONENTS;
D O I
10.3390/catal8010001
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Bio-oil reforming is considered for syngas or H-2 production. In this work, we studied the steam reforming (SR) of two raw bio-oils without adding external steam, using a recently-developed catalyst, Ni-UGSO. Experiments were performed at temperature (T) = 750850 degrees C and weight hourly space velocity (WHSV) = 1.77.1 g/gcat/h to assess C conversion (XC) and product yields. The results show that, in all conditions and with both bio-oils tested, the catalyst is stable for the entire duration of the tests (similar to 500 min) even when some C deposition occurred and that only at the highest WHSV tested there is a slight deactivation. In all tests, catalytic activity remained constant after a first, short, transient state, which corresponded to catalyst activation. The highest yields and conversions, with Y-H2, Y-CO and X-C of 94%, 84% and 100%, respectively, were observed at temperatures above 800 degrees C and WHSV = 1.7 g/g(cat)/h. The amount of H2O in the bio-oils had a non-negligible effect on catalyst activity, impacting Y-H2, Y-CO and X-C values. It was observed that, above a critical amount of H2O, the catalyst was not fully activated. However, higher H2O content led to the reduction of C deposits as well as lower Y-H2 and Y-CO and, through the water-gas-shift reaction, to higher Y-CO2 (CO2 selectivity). Fresh and spent catalysts were analyzed by physisorption (BET), X-ray diffraction, scanning electron microscopy and thermogravimetric analysis: the results reveal that, during the oils SR reaction, the initial spinel (Ni-Fe-Mg-Al) structures decreased over time-on-stream (TOS), while metallic Ni, Fe and their alloy phases appeared. Although significant sintering was observed in used catalysts, especially at high H2O/C ratio, the catalysts specific surface generally increased; the latter was attributed to the presence of nanometric metallic Ni and Ni-Fe alloy particles formed by reduction reactions. A small amount of C (4%) was formed at low H2O/C.
引用
收藏
页数:24
相关论文
共 50 条
  • [1] The 'Green' Ni-UGSO Catalyst for Hydrogen Production under Various Reforming Regimes
    Chamoumi, Mostafa
    Abatzoglou, Nicolas
    [J]. CATALYSTS, 2021, 11 (07)
  • [2] Deactivation of Ni spinel derived catalyst during the oxidative steam reforming of raw bio-oil
    Arandia, Aitor
    Remiro, Aingeru
    Valle, Beatriz
    Bilbao, Javier
    Gayubo, Ana G.
    [J]. FUEL, 2020, 276
  • [3] Catalytic steam reforming of bio-oil model compounds for hydrogen production over coal ash supported Ni catalyst
    Wang, Shurong
    Zhang, Fan
    Cai, Qinjie
    Li, Xinbao
    Zhu, Lingjun
    Wang, Qi
    Luo, Zhongyang
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (05) : 2018 - 2025
  • [4] Hydrogen Production by Low-temperature Steam Reforming of Bio-oil over Ni/HZSM-5 Catalyst
    Qiu, Song-bai
    Gong, Lu
    Liu, Lu
    Hong, Cheng-gui
    Yuan, Li-xia
    Li, Quan-xin
    [J]. CHINESE JOURNAL OF CHEMICAL PHYSICS, 2011, 24 (02) : 211 - 217
  • [5] Comparison of Ni Based and Rh Based Catalyst Performance in the Oxidative Steam Reforming of Raw Bio-Oil
    Remiro, Aingeru
    Arandia, Aitor
    Bilbao, Javier
    Gayubo, Ana G.
    [J]. ENERGY & FUELS, 2017, 31 (07) : 7147 - 7156
  • [6] Hydrogen production by steam reforming of bio-oil aqueous fraction over Ni/CeO2-ZrO2 catalyst
    Cheng, Feifei
    Hu, Rongrong
    Yan, Changfeng
    [J]. Taiyangneng Xuebao/Acta Energiae Solaris Sinica, 2011, 32 (07): : 1064 - 1068
  • [7] Hydrotreatment of bio-oil over Ni-based catalyst
    Zhang, Xinghua
    Wang, Tiejun
    Ma, Longlong
    Zhang, Qi
    Jiang, Ting
    [J]. BIORESOURCE TECHNOLOGY, 2013, 127 : 306 - 311
  • [8] Oxidative Steam Reforming of Raw Bio-Oil over Supported and Bulk Ni Catalysts for Hydrogen Production
    Arandia, Aitor
    Remiro, Aingeru
    Garcia, Veronica
    Castano, Pedro
    Bilbao, Javier
    Gayubo, Ana G.
    [J]. CATALYSTS, 2018, 8 (08)
  • [9] Effect of phenols extraction on the behavior of Ni-spinel derived catalyst for raw bio-oil steam reforming
    Valle, Beatriz
    Garcia-Gomez, Naiara
    Arandia, Aitor
    Remiro, Aingeru
    Bilbao, Javier
    Gayubo, Ana G.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (25) : 12593 - 12603
  • [10] Steam catalytic reforming of simulated bio-oil compounds with Ni and Fe supported by CaO catalyst for hydrogen production
    Wang, Zhibin
    Sun, Laizhi
    Chen, Lei
    Yang, Shuangxia
    Xie, Xinping
    Hua, Dongliang
    [J]. Taiyangneng Xuebao/Acta Energiae Solaris Sinica, 2022, 43 (02): : 16 - 21