Characterization of LaRhO3 perovskites for dry (CO2) reforming of methane (DRM)

被引:11
作者
Johansson, Ted [1 ]
Pakhare, Devendra [2 ]
Haynes, Daniel [3 ]
Abdelsayed, Victor [3 ]
Shekhawat, Dushyant [3 ]
Spivey, James [2 ]
机构
[1] Royal Inst Technol, Sch Chem Sci & Engn, SE-10044 Stockholm, Sweden
[2] Louisiana State Univ, Dept Chem Engn, Baton Rouge, LA 70803 USA
[3] US DOE, Natl Energy Technol Lab, Morgantown, WV 26507 USA
来源
CHEMICAL PAPERS | 2014年 / 68卷 / 09期
关键词
perovskite; LaRhO3; dry reforming of methane; temperature programmed reduction; temperature programmed surface reaction; ZIRCONATE PYROCHLORES LA2ZR2O7; SYNTHESIS GAS; SUBSTITUTION; TEMPERATURE; PERFORMANCE; REDUCTION; OXIDATION; CATALYSTS; RH;
D O I
10.2478/s11696-014-0566-2
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This work reports on the characterization of LaRhO3 perovskite as a catalyst for dry reforming of methane. The catalyst was studied using CH4-temperature programmed reduction (TPR), H-2-TPR, and temperature programmed surface reaction (TPSR), and the changes in the crystal structure of the catalyst due to these treatments were studied by X-ray diffraction (XRD). XRD pattern of the freshly calcined perovskites showed the formation of highly crystalline LaRhO3 and La2O3 phases. H-2-TPR of the fresh calcined catalyst showed a shoulder at 342A degrees C and a broad peak at 448A degrees C, suggesting that the reduction of Rh in perovskite occurs in multiple steps. XRD pattern of the reduced catalyst suggests complete reduction of the LaRhO3 phase and the formation of metallic Rh and minor amounts of La(OH)(3). The CH4-TPR data show qualitatively similar results as H-2-TPR, with a shoulder and a broad peak in the same temperature range. Following the H-2-TPR up to 950A degrees C, the same batch of catalyst was oxidized by flowing 5 vol. % O-2/He up to 500A degrees C and a second H-2-TPR (also up to 950A degrees C) was conducted. This second H-2-TPR differed significantly from that of the fresh calcined catalyst. The single sharp peak at 163A degrees C in the second H-2-TPR suggests a significant change in the catalyst, probably causedby the transformation of about 90 % of the perovskite into Rh/La2O3. This was confirmed by the XRD studies of the catalyst reduced after the oxidation at 500A degrees C. TPSR of the dry reforming reaction on the fresh calcined catalyst showed CO and H-2 formation starting at 400A degrees C, with complete consumption of the reactants at 650A degrees C. The uneven consumption of reactants between 400A degrees C and 650A degrees C suggests that reactions other than DRM occur, including reverse water gas shift (RWGS) and the Boudouard reaction (BR), probably as a result of in-situ changes in the catalyst, consistent with the H-2-TPR results. TPSR, after a H-2-TPR up to 950A degrees C, showed that the dry reforming reaction did not light off until 570A degrees C, which is much higher temperature than the one observed using fresh calcined catalyst. This shows that the uniform sites produced during the 950A degrees C H-2-TPR are catalytically less active than those of the fresh calcined catalyst, and that no significant side reactions such as RWGS or the Boudouard reaction occur. This suggests that reduction leads to the formation of a single type of sites which do not catalyze simultaneous side reactions.
引用
收藏
页码:1240 / 1247
页数:8
相关论文
共 22 条
  • [1] CO2 reforming of CH4
    Bradford, MCJ
    Vannice, MA
    [J]. CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1999, 41 (01): : 1 - 42
  • [2] Efficient catalytic abatement of greenhouse gases: Methane reforming with CO2 using a novel and thermally stable Rh-CeO2 catalyst
    Djinovic, Petar
    Batista, Jurka
    Pintar, Albin
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (03) : 2699 - 2707
  • [3] Gao J, 2011, FUEL CELLS: TECHNOLOGIES FOR FUEL PROCESSING, P191, DOI 10.1016/B978-0-444-53563-4.10007-0
  • [4] Catalytic partial oxidation of n-tetradecane using pyrochlores:: Effect of Rh and Sr substitution
    Haynes, Daniel J.
    Berry, David A.
    Shekhawat, Dushyant
    Spivey, James J.
    [J]. CATALYSIS TODAY, 2008, 136 (3-4) : 206 - 213
  • [5] Carbon dioxide reforming of methane to synthesis gas over LaNi1-xCrxO3 perovskite catalysts
    Kim, Joonho
    Kim, Taeyoon
    Yoo, Jung Whan
    Lee, Ki Bong
    Hong, Suk-In
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2012, 29 (10) : 1329 - 1335
  • [6] INTERACTION OF HYDROGEN WITH RH/LA2O3 AND PD/LA2O3 CATALYSTS
    KUZNETSOV, VL
    MUDRAKOVSKII, IL
    ROMANENKO, AV
    PASHIS, AV
    MASTIKHIN, VM
    YERMAKOV, YI
    [J]. REACTION KINETICS AND CATALYSIS LETTERS, 1984, 25 (1-2): : 137 - 141
  • [7] Effect of Partial Substitution of Ni by Cu in LaNiO3 Perovskite Catalyst for Dry Methane Reforming
    Moradi, G. R.
    Khosravian, F.
    Rahmanzadeh, M.
    [J]. CHINESE JOURNAL OF CATALYSIS, 2012, 33 (05) : 797 - 801
  • [8] Thermodynamic analysis of combined reforming process using Gibbs energy minimization method: In view of solid carbon formation
    Nematollahi, Behzad
    Rezaei, Mehran
    Lay, Ebrahim Nemati
    Khajenoori, Majid
    [J]. JOURNAL OF NATURAL GAS CHEMISTRY, 2012, 21 (06): : 694 - 702
  • [9] Effect of reaction temperature on activity of Pt- and Ru-substituted lanthanum zirconate pyrochlores (La2Zr2O7) for dry (CO2) reforming of methane (DRM)
    Pakhare, Devendra
    Shaw, Christopher
    Haynes, Daniel
    Shekhawat, Dushyant
    Spivey, James
    [J]. JOURNAL OF CO2 UTILIZATION, 2013, 1 : 37 - 42
  • [10] Characterization and activity study of the Rh-substituted pyrochlores for CO2 (dry) reforming of CH4
    Pakhare, Devendra
    Wu, Hongyi
    Narendra, Savinay
    Abdelsayed, Victor
    Haynes, Daniel
    Shekhawat, Dushyant
    Berry, David
    Spivey, James
    [J]. APPLIED PETROCHEMICAL RESEARCH, 2013, 3 (3-4): : 117 - 129