Volume 44 Issue 12
Dec.  2016
Turn off MathJax
Article Contents
WANG Bao-wei, MENG Da-jun, WANG Wei-han, LI Zhen-hua, MA Xin-bin. Effect of citric acid addition on MoO3/CeO2-Al2O3 catalyst for sulfur-resistant methanation[J]. Journal of Fuel Chemistry and Technology, 2016, 44(12): 1479-1484.
Citation: WANG Bao-wei, MENG Da-jun, WANG Wei-han, LI Zhen-hua, MA Xin-bin. Effect of citric acid addition on MoO3/CeO2-Al2O3 catalyst for sulfur-resistant methanation[J]. Journal of Fuel Chemistry and Technology, 2016, 44(12): 1479-1484.

Effect of citric acid addition on MoO3/CeO2-Al2O3 catalyst for sulfur-resistant methanation

Funds:

The project was supported by the National High Technology Research and Development Program of China 863计划,2015AA050504

More Information
  • Corresponding author: Tel: 021-23500806, wangbw@tju.edu.cn; Tel: 021-23500806, xbma@tju.edu.cn
  • Received Date: 2016-07-30
  • Rev Recd Date: 2016-09-29
  • Available Online: 2021-01-23
  • Publish Date: 2016-12-10
  • Citric acid hold great promise to improve the Mo-based catalyst performance for hydrogenation reaction applications. MoO3/CeO2-Al2O3 catalysts were prepared by impregnation method with adding citric acid into CeO2-Al2O3 composite supports and tested for sulfur resistant methanation. The syngas methanation activity increased with the increase of citric acid additive amount, and CO conversion could reach up 60% when the molar ratio of citric acid to Ce was 3. The prepared catalysts were characterized by BET, H2-TPR, XRD and XPS. The increased catalytic performance was mainly attributed to the increased amount of Ce species on the surface of catalysts which could decreased the interaction force between MoO3 and CeO2-Al2O3 supports. Additionally, the increased specific surface of CeO2-Al2O3 composite support was also in favor of catalytic performance.
  • loading
  • [1]
    KUSTOV A L,FREY A M,LARSEN K E,JOHANNESSEN T,NØRSKOV J K,CHRISTENSEN C H.CO methanation over supported bimetallic Ni-Fe catalysts:From computational studies towards catalyst optimization[J].Appl Catal A:Gen,2007,320(3):98-104. http://www.sciencedirect.com/science/article/pii/S0926860X06008969
    [2]
    KOPYSCINSKI J,SCHILDHAUER T J,BIOLLAZ S M A.Production of synthetic natural gas (SNG) from coal and dry biomass-A technology review from 1950 to 2009[J].Fuel,2010,89(8):1763-1783. doi: 10.1016/j.fuel.2010.01.027
    [3]
    HACATOGLU K,JAMES MCLELLAN P,LAYZELL D B.Production of bio-synthetic natural gas in Canada[J].Environ Sci Technol,2010,44(6):2183-2188. doi: 10.1021/es901561g
    [4]
    ZAHRADNIK R L,GLENN R A.Direct methanation of coal[J].Fuel,1971,50(1):77-90. doi: 10.1016/S0016-2361(71)81022-0
    [5]
    MOELLER F W,ROBERTS H,BRITZ B.Methanation of coal gas for SNG[J].Hydrocarbon Process,1974,53(4):69-74. https://www.researchgate.net/publication/283158569_METHANATION_OF_COAL_GAS_FOR_SNG
    [6]
    VEEN G V,KRUISSINK E C,DOESBURG E B M,ROSS J R H,REIJEN L L V.The effect of preparation conditions on the activity and stability of copreciptitated Ni/Al2O3 catalysts for the methanation of carbon monoxide[J].React Kinet Catal Lett,1978,9(2):143-148. doi: 10.1007/BF02068914
    [7]
    GALLAGHER J E,EUKER C A.Catalytic coal gasification for SNG manufacture[J].Int J Energy Res,1980,4(2):137-147. doi: 10.1002/(ISSN)1099-114X
    [8]
    FRANK A J,DICK H A,GORAL J,NELSON A J,GRÄTZEL M.MoS2-catalyzed methanation of CO with H2S[J].J Catal,1990,126(2):674-676. doi: 10.1016/0021-9517(90)90030-N
    [9]
    CHRISTENSEN J M,MORTENSEN P M,TRANE R,JENSEN P A,JENSEN A D.Effects of H2S and process conditions in the synthesis of mixed alcohols from syngas over alkali promoted cobalt-molybdenum sulfide[J].Appl Catal A:Gen,2009,366(1):29-43. doi: 10.1016/j.apcata.2009.06.034
    [10]
    KIM M Y,HA S B,DONG J K,BYUN C,PARK E D.CO methanation over supported Mo catalysts in the presence of H2S[J].Catal Commun,2013,35(17):68-71.
    [11]
    SASAKI T,SUZUKI T.Sulfide molybdenum catalysts for water-gas shift reaction:Influence of the kind of promoters and supports to generate MoS2[J].Appl Catal A:Gen,2014,484(10):79-83.
    [12]
    WANG B W,DING G Z,SHANG Y G,LV J,WANG H Y,WANG E D,LI Z H,MA X B,QIN S D,SUN Q.Effects of MoO3 loading and calcination temperature on the activity of the sulphur-resistant methanation catalyst MoO3/γ-Al2O3[J].Appl Catal A:Gen,2012,431-432:144-150. doi: 10.1016/j.apcata.2012.04.029
    [13]
    TRIKI M,KSIBI Z,GHORBEL A,MEDINA F.Preparation and characterization of CeO2-Al2O3 aerogels supported ruthenium for catalytic wet air oxidation of p-hydroxybenzoic acid[J].J Sol-Gel Sci Technol,2011,59(1):1-6. doi: 10.1007/s10971-011-2452-5
    [14]
    [15]
    YAO H C,YAO Y F Y.Ceria in automotive exhaust catalysts:I.Oxygen storage[J].J Catal,1984,86(2):254-265. doi: 10.1016/0021-9517(84)90371-3
    [16]
    ZHUANG Q,QIN Y,CHANG L.Promoting effect of cerium oxide in supported nickel catalyst for hydrocarbon steam-reforming[J].Appl Catal,1991,70(1):1-8. doi: 10.1016/S0166-9834(00)84149-4
    [17]
    WANG B W,SHANG Y G,DING G Z,LÜ J,WANG H Y,WANG E D,LI Z H,MA X B,QIN S D,SUN Q.Effect of the ceria-alumina composite support on the Mo-based catalyst's sulfur-resistant activity for the synthetic natural gas process[J].Reac Kinet,Mech Cat,2012,106(2):495-506. doi: 10.1007/s11144-012-0452-2
    [18]
    CATTANEO R,WEBER T,SHIDO T,PRINS R.A quick EXAFS study of the sulfidation of NiMo/SiO2 hydrotreating catalysts prepared with chelating ligands[J].J Catal,2000,191(1):225-236. doi: 10.1006/jcat.1999.2784
    [19]
    IWAMOTO R,KAGAMI N,ⅡNO A.Effect of polyethylene glycol addition on hydrodesulfurization activity over CoO-MoO3/Al2O3 catalyst[J].J Jpn Pet Inst,2005,48(4):237-242. doi: 10.1627/jpi.48.237
    [20]
    RINALDI N,KUBOTA T,OKAMOTO Y.Effect of citric acid addition on Co-Mo/B2O3/Al2O3 catalysts prepared by a post-treatment method[J].Ind Eng Chem Res,2009,48(23):10414-10424. doi: 10.1021/ie9008343
    [21]
    LI H F,LI M F,CHU Y,LIU F,NIE H.Essential role of citric acid in preparation of efficient NiW/Al2O3 HDS catalysts[J].Appl Catal A:Gen,2011,403(1/2):75-82. http://www.doc88.com/p-1931584301169.html
    [22]
    CASTILLO-VILLALÓN P,RAMIREZ J,VARGAS-LUCIANO J A.Analysis of the role of citric acid in the preparation of highly active HDS catalysts[J].J Catal,2014,320(1):127-136. https://www.researchgate.net/publication/267456000_Analysis_of_the_role_of_citric_acid_in_the_preparation_of_highly_active_HDS_catalysts
    [23]
    BERGWERFF J A,JANSEN M,LELIVELD B G,VISSER T,JONG K P D,WECKHUYSEN B M.Influence of the preparation method on the hydrotreating activity of MoS2/Al2O3 extrudates:A Raman microspectroscopy study on the genesis of the active phase[J].J Catal,2006,243(2):292-302. doi: 10.1016/j.jcat.2006.07.022
    [24]
    RINALDI N,KUBOTA T,OKAMOTO Y.Effect of citric acid addition on the hydrodesulfurization activity of MoO3/Al2O3 catalysts[J].Appl Catal A:Gen,2010,374(1/2):228-236.
    [25]
    WANG R,SMITH K J.Hydrodesulfurization of 4,6-dimethyldibenzothiophene over high surface area metal phosphides[J].Appl Catal A:Gen,2009,361(1):18-25. https://www.researchgate.net/publication/239691379_Hydrodesulfurization_of_46-dimethyldibenzothiophene_over_high_surface_area_metal_phosphides
    [26]
    SURESH R,PONNUSWAMY V,MARIAPPAN R.Effect of annealing temperature on the microstructural,optical and electrical properties of CeO2 nanoparticles by chemical precipitation method[J].Appl Surf Sci,2013,273(273):457-464. https://www.researchgate.net/publication/257032897_Effect_of_annealing_temperature_on_the_microstructural_optical_and_electrical_properties_of_CeO2_nanoparticles_by_chemical_precipitation_method
    [27]
    LIANG C X,LI X Y,QU Z P,TADE M,LIU S M.The role of copper species on Cu/γ-Al2O3 catalysts for NH3-SCO reaction[J].Appl Surf Sci,2012,258(8):3738-3743. doi: 10.1016/j.apsusc.2011.12.017
    [28]
    MESTL G,SRINIVASAN T K K,KNOEZINGER H.Mechanically activated MoO3.3.Characterization by vibrational spectroscopy[J].Langmuir,2002,11(10):3795-3804.
    [29]
    MESTL G,SRINIVASAN T K K.Raman spectroscopy of monolayer-type catalysts:Supported molybdenum oxides[J].Cat Rev,1998,40(4):451-570. doi: 10.1080/01614949808007114
    [30]
    ABERUAGBA F,KUMAR M,MURALIDHAR G,SHARMA L D.Characterization of Al2O3-ZrO2 mixed oxide supported Mo hydrotreating catalyst[J].Pet Sci Technol,2004,22(9):1287-1298.
    [31]
    ZAKI M I,VIELHABER B,KNOEZINGER H.Low-temperature carbon monoxide adsorption and state of molybdena supported on alumina,titania,ceria,and zirconia.An infrared spectroscopic investigation[J].J Phys Chem,1986,90(14):3176-3183. doi: 10.1021/j100405a026
    [32]
    BERIT H,NØRSKOV J K,HENRIK T E.A density functional study of the chemical differences between Type I and Type Ⅱ MoS2-based structures in hydrotreating catalysts[J].J Phys Chem B,2005,109(6):2245-2253. doi: 10.1021/jp048842y
  • 加载中

Catalog

    通讯作者: 陈斌, bchen63@163.com
    • 1. 

      沈阳化工大学材料科学与工程学院 沈阳 110142

    1. 本站搜索
    2. 百度学术搜索
    3. 万方数据库搜索
    4. CNKI搜索

    Article Metrics

    Article views (73) PDF downloads(9) Cited by()
    Proportional views
    Related

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return