Steam reforming reactions over a metal-monolithic anodic alumina-supported Ni catalyst with trace amounts of noble metal

被引:32
作者
Guo, Yu [1 ]
Thou, Lu [1 ]
Kameyama, Hideo [1 ]
机构
[1] Tokyo Univ Agr & Technol, Kameyama Lab, Dept Chem Engn, Koganei, Tokyo 1848588, Japan
关键词
Hydrocarbon steam reforming; Anodic alumina support; Nickel catalyst; Noble metal addition; Steam purge treatment; SELF-REGENERATIVE ACTIVITY; SHUT-DOWN OPERATION; DSS-LIKE OPERATION; DAILY START-UP; NI/MG(AL)O CATALYSTS; NICKEL-CATALYSTS; DOPED NI/MG(AL)O; CARBON-DIOXIDE; METHANE; PLATE;
D O I
10.1016/j.ijhydene.2011.02.069
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A trace amount of noble metal (Ru or Pt <0.1 wt%) was doped onto an anodic alumina-supported Ni catalyst, to investigate its performance in the steam reforming of methane (SRM), especially during DSS (daily startup and shutdown) operation. Although the steam purge treatment at high temperatures seriously deactivated the Ni catalyst because of the oxidation of metallic nickel with steam into Ni(2+), trace Ru assisted the regeneration of active metallic nickel by hydrogen-spillover. And, the Ni sintering was largely alleviated by the addition of Ru, and it was probably due to the formation of Ru Ni alloy. In comparison with the Ru-doped Ni catalyst, the Pt-doped Ni catalyst showed a more favorable tolerance to steam oxidation, even at 900 degrees C. In a stationary SRM test of 3000 h and a DSS SRM test of 500 times where the town gas 13A was used as hydrogen source, no obvious deterioration was detected over the Pt-doped Ni catalyst. Especially, when electrically heating the plate-type Pt-doped Ni catalyst to 700 degrees C, the SRM reaction system could reach a stable state within ca. 10 mm, which offered a strong possibility to shorten the startup time from the 1-2 h of conventional reformer to just few minutes. In addition, the noble metal-doped Ni catalyst also showed favorable activity and durability when being applied to other steam reforming systems, such as kerosene and ethanol. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:5321 / 5333
页数:13
相关论文
共 35 条
[1]   ON THE ROLE OF A NIAL2O4 INTERMEDIATE LAYER IN THE SINTERING BEHAVIOR OF NI/ALPHA-AL2O3 [J].
BOLT, PH ;
HABRAKEN, FHPM ;
GEUS, JW .
JOURNAL OF CATALYSIS, 1995, 151 (02) :300-306
[2]   CONVERSION OF METHANE AND CARBON-DIOXIDE INTO SYNTHESIS GAS OVER ALUMINA-SUPPORTED NICKEL-CATALYSTS - EFFECT OF NI-AL2O3 INTERACTIONS [J].
CHEN, YG ;
REN, J .
CATALYSIS LETTERS, 1994, 29 (1-2) :39-48
[3]   Production of hydrogen for fuel cells by reformation of biomass-derived ethanol [J].
Fatsikostas, AN ;
Kondarides, DI ;
Verykios, XE .
CATALYSIS TODAY, 2002, 75 (1-4) :145-155
[4]  
FUJU A, 2005, SANYO TECH REV, V37, P69
[5]   Characterization of performances of the wall-type reactor with plate-fin type nickel catalyst prepared by electroless plating, for methanol decomposition [J].
Fukuhara, C ;
Igarashi, A .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2004, 37 (03) :415-421
[6]   Dry reforming of methane over nickel catalysts supported on magnesium aluminate spinels [J].
Guo, JJ ;
Lou, H ;
Zhao, H ;
Chai, DF ;
Zheng, XM .
APPLIED CATALYSIS A-GENERAL, 2004, 273 (1-2) :75-82
[7]   Steam Methane Reforming Using an Anodic Alumina Supported Nickel Catalyst (Ni/Al2O3/Alloy): Analysis of Catalyst Deactivation [J].
Guo, Yu ;
Thanh Phong Tran ;
Zhou, Lu ;
Zhang, Qi ;
Kameyama, Hideo .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2007, 40 (13) :1221-1228
[8]   A novel KCaNi/α-Al2O3 catalyst for CH4 reforming with CO2 [J].
Hou, ZY ;
Yokota, O ;
Tanaka, T ;
Yashima, T .
CATALYSIS LETTERS, 2003, 87 (1-2) :37-42
[9]   Preparation and application of nickel-containing smectite-type clay materials for methane reforming with carbon dioxide [J].
Iwasa, Nobuhiro ;
Takizawa, Masanori ;
Arai, Masahiko .
APPLIED CATALYSIS A-GENERAL, 2006, 314 (01) :32-39
[10]   Ru-doped Ni catalysts effective for the steam reforming of methane without the pre-reduction treatment with H2 [J].
Jeong, JH ;
Lee, JW ;
Seo, DJ ;
Seo, Y ;
Yoon, WL ;
Lee, DK ;
Kim, DH .
APPLIED CATALYSIS A-GENERAL, 2006, 302 (02) :151-156