Hydrogen rich syngas from CO2 reforming of methane with steam catalysed by facile fusion-impregnation of iron and cobalt loaded MgAl2O4 catalyst with minimal carbon deposits

被引:17
|
作者
Rahmat, Norhasyimi [1 ]
Yaakob, Zahira [2 ]
Hassan, Nik Suhaimi Mat [3 ]
机构
[1] Univ Teknol MARA, Fac Chem Engn, Shah Alam 40450, Selangor, Malaysia
[2] Univ Kebangsaan Malaysia, Res Ctr Sustainable Proc Technol CESPRO, Fac Engn & Built Environm, Bangi 43600, Selangor, Malaysia
[3] Sime Darby Res Sdn Bhd, Res & Dev Ctr, Carey Isl 42960, Selangor, Malaysia
关键词
Fe/MgAl2O4; Co/MgAl2O4; Fusion-impregnation; CO2; reforming; Coke deposition resistance; MODEL BIOGAS; FE; REDUCTION; SORPTION;
D O I
10.1016/j.joei.2021.02.001
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The newly synthesised catalysts via facile fusion-impregnation of iron and cobalt onto MgAl2O4 were successfully accomplished with relatively high surface area and pore volume which exhibited mesoporous structure with narrow pore distribution. These catalysts were employed for CO2 reforming of CH4 with steam which was carried out at different reaction temperatures of 700, 750, 800, 850 and 900 degrees C. Different metal loadings of cobalt at 5, 15, 25, 40 and 50 wt% were also synthesised to study the effect of catalytic activity on CH4 and CO2 conversion as well as H-2 yield. It was observed that CH4 and CO2 conversion achieved its highest value at Co loading of 25 wt%. Addition of steam, basic properties, lattice textural of MgAl2O4 and magnesium metal oxides were suggested to be factors that keep out the coke formation on catalyst surface. However, the metal loading of more than 40 wt% Co started to show declination of catalyst activity and formation carbon deposits on catalyst surface. This circumstance suggests an agglomerated particle condition that decreases the active sites and hampers the gasification of carbon on catalyst surface. Possible reaction pathways are proposed in this study to elucidate the engagement of Fe and Co in CH4 and CO2 activation as well as their combination with surface carbon which further eliminates the coke deposition. The removal of carbon by oxidation was examined by XRD, TEM, TPO, Raman spectroscopy and TGA, which concludes its mechanism through oxidation of metal particles and surface carbon gasification from lattice oxygen. (C) 2021 Energy Institute. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:61 / 74
页数:14
相关论文
共 50 条
  • [41] Carbon deposition and catalyst stability over La2NiO4/γ-Al2O3 during CO2 reforming of methane to syngas
    Liu, BS
    Au, CT
    APPLIED CATALYSIS A-GENERAL, 2003, 244 (01) : 181 - 195
  • [42] Effect of the water-ethanol molar ratio in the ethanol steam reforming reaction over a Co/CeO2/MgAl2O4 catalyst
    Barroso, Mariana N.
    Gomez, Manuel F.
    Arrua, Luis A.
    Abello, Maria C.
    REACTION KINETICS MECHANISMS AND CATALYSIS, 2015, 115 (02) : 535 - 546
  • [43] Effect of higher alcohols on the performances of a 1%Rh/MgAl2O4/Al2O3 catalyst for hydrogen production by crude bioethanol steam reforming
    Le Valant, Anthony
    Garron, Anthony
    Bion, Nicolas
    Duprez, Daniel
    Epron, Florence
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (01) : 311 - 318
  • [44] Syngas production from CO2 reforming of methane over ceria supported cobalt catalyst: Effects of reactants partial pressure
    Ayodele, Bamidele V.
    Khan, Maksudur R.
    Cheng, Chin Kui
    JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2015, 27 : 1016 - 1023
  • [45] Combined steam and CO2 reforming of methane (CSCRM) over Ni-Pd/Al2O3 catalyst for syngas formation
    Batebi, Dania
    Abedini, Reza
    Mosayebi, Amir
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2020, 45 (28) : 14293 - 14310
  • [46] Effects of Nickel Precursor and Calcination Temperature on the Performance of Ni/MgAl2O4 Catalysts for Syngas Production by CO2 Reforming of Coke Oven Gas
    Zhou, Huijie
    Cheng, Hongwei
    Wu, Cheng
    Lu, Xionggang
    4TH ANNUAL INTERNATIONAL WORKSHOP ON MATERIALS SCIENCE AND ENGINEERING (IWMSE2018), 2018, 381
  • [47] Combined H2O and CO2 reforming of coke oven gas over Ca-promoted Ni/MgAl2O4 catalyst for direct reduced iron production
    Koo, Kee Young
    Lee, Jin Hyang
    Jung, Un Ho
    Kim, Sung Hyun
    Yoon, Wang Lai
    FUEL, 2015, 153 : 303 - 309
  • [48] The promotional effect of K on the catalytic activity of Ni/MgAl2O4 for the combined H2O and CO2 reforming of coke oven gas for syngas production
    Jin Hyang Lee
    Kee Young Koo
    Un Ho Jung
    Ji Eun Park
    Wang Lai Yoon
    Korean Journal of Chemical Engineering, 2016, 33 : 3115 - 3120
  • [49] The promotional effect of K on the catalytic activity of Ni/MgAl2O4 for the combined H2O and CO2 reforming of coke oven gas for syngas production
    Lee, Jin Hyang
    Koo, Kee Young
    Jung, Un Ho
    Park, Ji Eun
    Yoon, Wang Lai
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2016, 33 (11) : 3115 - 3120
  • [50] The effect of CO2 feeding on syngas quality in autothermal reforming of methane over Ni-Al2O3 catalyst: possibility of CO2 conversion to hydrogen
    E. Aryafard
    M. Farsi
    A. R. Alipoor
    M. R. Rahimpour
    Reaction Kinetics, Mechanisms and Catalysis, 2023, 136 : 671 - 687