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

被引:191
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
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 33 条
  • [1] [Anonymous], 2006, KINETICS CATALYSIS M
  • [2] Absorption of H2S andCO2 in alkanolamine aqueous solution:: Experimental data and modelling with the electrolyte-NRTL model
    Barreau, A.
    le Bouhelec, E. Blanchon
    Tounsi, K. N. Habchi
    Mougin, P.
    Lecomte, F.
    [J]. OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2006, 61 (03): : 345 - 361
  • [3] Butwell F.B., 1975, LAUR REID GAS COND C
  • [4] Simultaneous steam and CO2 reforming of methane to syngas over NiO/MgO/SA-5205 in presence and absence of oxygen
    Choudhary, VR
    Uphade, BS
    Mamman, AS
    [J]. APPLIED CATALYSIS A-GENERAL, 1998, 168 (01) : 33 - 46
  • [5] Heijungs R., 1992, Environmental Life Cycle Assessment of Products: Guide and Backgrounds
  • [6] Syngas by catalytic partial oxidation of methane on rhodium: Mechanistic conclusions from spatially resolved measurements and numerical simulations
    Horn, R.
    Williams, K. A.
    Degenstein, N. J.
    Schmidt, L. D.
    [J]. JOURNAL OF CATALYSIS, 2006, 242 (01) : 92 - 102
  • [7] Addition effect of ruthenium on nickel steam reforming catalysts
    Ishihara, A
    Qian, EW
    Finahari, IN
    Sutrisna, IP
    Kabe, T
    [J]. FUEL, 2005, 84 (12-13) : 1462 - 1468
  • [8] Steam and CO2 reforming of methane over a Ru/ZrO2 catalyst
    Jakobsen, Jon Geest
    Jorgensen, Tommy L.
    Chorkendorff, Ib
    Sehested, Jens
    [J]. APPLIED CATALYSIS A-GENERAL, 2010, 377 (1-2) : 158 - 166
  • [9] Krause T., 2002, AM I CHEM ENG SPRING
  • [10] Kugler E. L., 2012, METHANE REFORMING CA