Preparation and characterisation of γ-Al2O3 particles-supported Rh/Ce0.9Pr0.1O2 catalyst for N2O decomposition in the presence of O2, H2O and NOx

被引:21
|
作者
Parres-Esclapez, S. [1 ]
Illan-Gomez, M. J. [1 ]
Salinas-Martinez de Lecea, C. [1 ]
Bueno-Lopez, A. [1 ]
机构
[1] Univ Alicante, Dept Inorgan Chem, E-03080 Alicante, Spain
关键词
N2O decomposition; Rh; Ceria; gamma-Al2O3; In situ DRIFTS; SURFACE-AREA; X-RAY; REDUCTION; OXIDE; PR; PERFORMANCE; ADSORPTION; RH/CEO2; RAMAN; SIZE;
D O I
10.1016/j.ijggc.2012.09.003
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A supported catalyst composed by the active phase Rh/Ce0.9Pr0.1O2 loaded on gamma-Al2O3 particles was prepared and characterised by SEM, TEM, XRD, Raman spectroscopy, N-2 adsorption at -196 degrees C, H-2-TPR and XPS. The catalytic decomposition of N2O was studied in simulated nitric acid plant streams (in the presence of O-2, H2O and/or NOx) both in a fix-bed reactor and by in situ DRIFTS-MS experiments. The supported catalyst is able to decompose N2O from around 350-400 degrees C in the presence of O-2, H2O and/or NOx, and this temperature would be enough to decompose N2O in a nitric acid production plant after the expansion turbine, avoiding the use of an additional energy input. Among O-2, H2O and NOx, NOx is the strongest inhibitor and O-2 the weakest. The inhibiting effect of O-2 is attributed to its reversible chemisorption on catalyst active sites, while the effect of H2O and NOx is mainly related with their irreversible chemisorption. The inhibition of H2O is not as high as that of NOx because the product of H2O chemisorption (Ce-OH surface groups) is suitable for N2O chemisorption and decomposition, while the surface nitrogen species created upon NOx chemisorption are not. (c) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:251 / 261
页数:11
相关论文
共 50 条
  • [31] Peristaltic transport of γAl2O3/H2O and γAl2O3/C2H6O2 in an asymmetric channel
    Salahuddin, T.
    Khan, Muhammad Habib Ullah
    Arshad, Maryam
    Abdel-Sattar, M. A.
    Elmasry, Yasser
    JOURNAL OF MATERIALS RESEARCH AND TECHNOLOGY-JMR&T, 2020, 9 (04): : 8337 - 8349
  • [32] Fe2O3/Al2O3 catalysts for the N2O decomposition in the nitric acid industry
    Giecko, Grzegorz
    Borowiecki, Tadeusz
    Gac, Wojciech
    Kruk, Janusz
    CATALYSIS TODAY, 2008, 137 (2-4) : 403 - 409
  • [33] KINETICS OF THE CO OXIDATION BY O2 AND N2O OVER CU-CR/AL2O3
    DEKKER, NJJ
    HOORN, JAA
    STEGENGA, S
    KAPTEIJN, F
    MOULIJN, JA
    AICHE JOURNAL, 1992, 38 (03) : 385 - 396
  • [34] INTERACTION OF O2, N2O, NO, AND CO WITH FE(II, III) OXIDES DEPOSITED ON AL2O3
    YASKEVICH, VI
    KOTOVA, GN
    ALEKSEEVA, GK
    KINETICS AND CATALYSIS, 1990, 31 (04) : 883 - 886
  • [35] An IR study on the surface passivation of Mo2C/Al2O3 catalyst with O2, H2O and CO2
    Wu, WC
    Wu, ZL
    Liang, CH
    Ying, PL
    Feng, ZC
    Li, C
    PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2004, 6 (24) : 5603 - 5608
  • [36] Enhancement of N2O decomposition performance by N2O pretreatment over Ce-Co-O catalyst
    You, Yanchen
    Chang, Huazhen
    Ma, Lei
    Guo, Lei
    Qin, Xuan
    Li, Jiayin
    Li, Junhua
    CHEMICAL ENGINEERING JOURNAL, 2018, 347 : 184 - 192
  • [37] Enhancement of N2O decomposition performance by N2O pretreatment over Ce-Co-O catalyst
    Chang, Huazhen (chz@ruc.edu.cn), 1600, Elsevier B.V., Netherlands (347):
  • [38] The Influence Of NO/O2 On The NOx Storage Properties Over A Pt-Ba-Ce/γ-Al2O3 Catalyst
    Feng, Xuedong
    Yi, Jing
    Luo, Peng
    OPEN CHEMISTRY, 2019, 17 (01): : 1459 - 1465
  • [39] Catalytic decomposition of N2O and catalytic reduction of N2O and N2O+NO by NH3 in the presence of O2 over Fe-zeolite
    Guzmán-Vargas, A
    Delahay, G
    Coq, B
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 42 (04) : 369 - 379
  • [40] Structures and binding energies of O2-•H2O and O2•H2O
    Bell, AJ
    Wright, TG
    PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2004, 6 (18) : 4385 - 4390