Biogas reforming for syngas production over nickel supported on ceria-alumina catalysts

被引:127
|
作者
Bereketidou, O. A. [1 ,2 ,3 ]
Goula, M. A. [1 ]
机构
[1] Technol Educ Inst Western Macedonia, Pollut Control Technol Dept, GR-50100 Koila, Kozani, Greece
[2] Univ Western Macedonia, Dept Mech Engn, GR-50100 Bakola, Kozani, Greece
[3] Univ Western Macedonia, Dept Mech Engn, GR-50100 Sialvera, Kozani, Greece
关键词
Biogas reforming; Nickel catalysts; Syngas production; Ceria-alumina; HYDROGEN-PRODUCTION; NI CATALYSTS; SYNTHESIS GAS; NOBLE-METALS; MIXED OXIDES; METHANE; CO2; SURFACE; CH4; DEACTIVATION;
D O I
10.1016/j.cattod.2012.07.006
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A series of 8 wt% nickel catalysts supported on alumina and alumina-modified with different amounts of ceria were prepared. The effect of the supporting ceria loading at the catalytic performance for the biogas reforming reaction was investigated. The physicochemical properties of the final catalysts were determined by using different techniques: N-2 adsorption-desorption isotherms, X-ray diffraction (XRD), inductively coupled plasma atomic emission spectroscopy (ICP-AES) and transmission electron microscopy (TEM). Catalytic performance was evaluated for the biogas reforming reaction using a feed gas mixture of CH4/CO2 = 1.5, simulating a clean model of biogas. It was shown that nickel catalysts supported on ceria-alumina exhibit slightly higher conversion values, compared to the one supported on alumina above 800 degrees C, which can be mainly attributed to the redox properties of ceria. In particular, the 8 wt% nickel catalyst supported on 20 wt% ceria-alumina was proven to have the best catalytic performance with a highest H-2/CO ratio of about 1.3. The biogas reforming reaction catalyzed by nickel-alumina doped with ceria catalysts seems to be an appropriate process in order to produce syngas suitable for methanol or Fischer-Tropsch synthesis reactions, which require H-2/CO ratio values between one and two (1 to 2). (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:93 / 100
页数:8
相关论文
共 50 条
  • [1] Steam reforming of methanol over ruthenium impregnated ceria, alumina and ceria-alumina catalysts
    Aouad, Samer
    Gennequin, Cedric
    Mrad, Mary
    Tidahy, Haingomalala Lucette
    Estephane, Jane
    Aboukais, Antoine
    Abi-Aad, Edmond
    [J]. INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2016, 40 (09) : 1287 - 1292
  • [2] Effects of synthesis route on the performance of mesoporous ceria-alumina and ceria-zirconia-alumina supported nickel catalysts in steam and autothermal reforming of diesel
    Bozda, Arzu Arslan
    Sezgi, Naime Asli
    Dogu, Timur
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2022, 47 (07) : 4568 - 4583
  • [3] Experimental Investigation on Biogas Reforming for Syngas Production over an Alumina Based Nickel Catalyst
    Rathod, Vikram
    Bhale, Purnanand V.
    [J]. 4 INTERNATIONAL CONFERENCE ON ADVANCES IN ENERGY RESEARCH (ICAER 2013), 2014, 54 : 236 - 245
  • [4] Biogas reforming for hydrogen enrichment by ceria decorated over nickel catalyst supported on titania and alumina
    Rosha, Pali
    Mohapatra, Saroj Kumar
    Mahla, Sunil Kumar
    Dhir, Amit
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (46) : 21246 - 21255
  • [5] Preferential CO oxidation over nanosized gold catalysts supported on ceria and amorphous ceria-alumina
    Fonseca, Juliana
    Royer, Sebastien
    Bion, Nicolas
    Pirault-Roy, Laurence
    Rangel, Maria do Carmo
    Duprez, Daniel
    Epron, Florence
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2012, 128 : 10 - 20
  • [6] Direct conversion of biogas to syngas over bimetallic nickel-cobalt supported on α-alumina catalysts
    Thirumalarasu, Bhalamphiga Arasi
    Rajagopalan, Aravindh
    Murugan, Swetha
    Ragula, Udaya Bhaskar Reddy
    [J]. RENEWABLE ENERGY, 2024, 234
  • [7] Hydrogen production and coke minimization through reforming of kerosene over bi-metallic ceria-alumina supported Ru-Ni catalysts
    Kaynar, A. Derya Deniz
    Dogu, Doruk
    Yasyerli, Nail
    [J]. FUEL PROCESSING TECHNOLOGY, 2015, 140 : 96 - 103
  • [8] Steam Reforming of Glycerol for Hydrogen Production Over Supported Nickel Catalysts on Alumina
    Choi, Ga Young
    Kim, Young Chul
    Moon, Dong Ju
    Seo, Gon
    Park, Nam Cook
    [J]. JOURNAL OF NANOSCIENCE AND NANOTECHNOLOGY, 2013, 13 (01) : 653 - 656
  • [9] Syngas Production via Methane Dry Reforming over Ceria-Magnesia Mixed Oxide-Supported Nickel Catalysts
    Al-Swai, Basem M.
    Osman, Noridah
    Alnarabiji, Mohamad Sahban
    Adesina, Adesoji A.
    Abdullah, Bawadi
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2019, 58 (02) : 539 - 552
  • [10] H2 production from catalytic steam reforming of n-propanol over ruthenium and ruthenium-nickel bimetallic catalysts supported on ceria-alumina oxides with different ceria loadings
    Wang, Meng
    Au, Chak-Tong
    Lai, Suk-Yin
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (40) : 13926 - 13935