Evaluation of the economic and environmental impact of combining dry reforming with steam reforming of methane

被引:190
|
作者
Gangadharan, Preeti [1 ]
Kanchi, Krishna C. [1 ]
Lou, Helen H. [1 ]
机构
[1] Lamar Univ, Dan F Smith Dept Chem Engn, Beaumont, TX 77710 USA
来源
关键词
Dry reforming; Syngas; Steam methane reforming; Global warming potential; CO2; ABSORPTION; KINETICS; RHODIUM; SYNGAS; NICKEL;
D O I
10.1016/j.cherd.2012.04.008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Lately, there has been considerable interest in the development of more efficient processes to generate syngas, an intermediate in the production of fuels and chemicals, including methanol, dimethyl ether, ethylene, propylene and Fischer-Tropsch fuels. Steam methane reforming (SMR) is the most widely applied method of producing syngas from natural gas. Dry reforming of methane (DRM) is a process that uses waste carbon dioxide to produce syngas from natural gas. Dry reforming alone has not yet been implemented commercially; however, a combination of steam methane reforming and dry reforming of methane (SMR + DRM) has been used in industry for several years. The aim of this work was to simulate both the SMR and SMR + DRM processes and to conduct an economic and environmental analysis to determine whether the SMR + DRM process is competitive with the more popular SMR process. The results indicate that the SMR + DRM process has a lower carbon footprint. Further research on DRM catalysts could make this process economically competitive with steam methane reforming. (C) 2012 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1956 / 1968
页数:13
相关论文
共 50 条
  • [41] Structured catalysts for dry reforming of methane
    Nair, Mahesh Muraleedharan
    Kaliaguine, Serge
    NEW JOURNAL OF CHEMISTRY, 2016, 40 (05) : 4049 - 4060
  • [42] Control of parallel dry methane and steam methane reforming processes for Fischer-Tropsch syngas
    Luyben, William L.
    JOURNAL OF PROCESS CONTROL, 2016, 39 : 77 - 87
  • [43] Dry reforming of methane has no future for hydrogen production: Comparison with steam reforming at high pressure in standard and membrane reactors
    Oyama, S. Ted
    Hacarlioglu, Pelin
    Gu, Yunfeng
    Lee, Doohwan
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (13) : 10444 - 10450
  • [44] Stabilizing catalysts for dry reforming of methane
    Littlewood, Patrick
    Stair, Peter
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2018, 255
  • [45] Kinetic behaviour of commercial catalysts for methane reforming in ethanol steam reforming process
    Jorge Vicente
    Javier Erea
    Martin Olazar
    Pedro LBenito
    Javier Bilbao
    Ana GGayubo
    Journal of Energy Chemistry, 2014, 23 (05) : 639 - 644
  • [46] Characterization and evaluation of Ni-based pyrochlore for the steam reforming of methane
    Haynes, Daniel
    Shekhawat, Dushyant
    Berry, David
    Smith, Mark
    Baltrus, John
    Spivey, James
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2016, 251
  • [47] Kinetic behaviour of commercial catalysts for methane reforming in ethanol steam reforming process
    Vicente, Jorge
    Erena, Javier
    Olazar, Martin
    Benito, Pedro L.
    Bilbao, Javier
    Gayubo, Ana G.
    JOURNAL OF ENERGY CHEMISTRY, 2014, 23 (05) : 639 - 644
  • [48] Kinetic behaviour of commercial catalysts for methane reforming in ethanol steam reforming process
    Jorge Vicente
    Javier Erea
    Martin Olazar
    Pedro L.Benito
    Javier Bilbao
    Ana G.Gayubo
    Journal of Energy Chemistry, 2014, (05) : 639 - 644
  • [49] Scaleable, microstructured plant for steam reforming of methane
    Seris, E. L. C.
    Abramowitz, G.
    Johnston, A. M.
    Haynes, B. S.
    CHEMICAL ENGINEERING JOURNAL, 2008, 135 : S9 - S16
  • [50] Production of hydrogen by unmixed steam reforming of methane
    Dupont, V.
    Ross, A. B.
    Knight, E.
    Hanley, I.
    Twigg, M. V.
    CHEMICAL ENGINEERING SCIENCE, 2008, 63 (11) : 2966 - 2979