Activity of rhodium-based catalysts for CO preferential oxidation in H2-rich gases

被引:25
作者
Galletti, C. [1 ]
Fiorot, S. [1 ]
Specchia, S. [1 ]
Saracco, G. [1 ]
Specchia, V. [1 ]
机构
[1] Politecn Torino, Dept Mat Sci & Chem Engn, I-10129 Turin, Italy
关键词
hydrogen gas mixture clean-up; CO preferential oxidation; Rh-based catalyst; CARBON-MONOXIDE; FUEL PROCESSOR; HYDROGEN; RU/GAMMA-AL2O3; PERFORMANCE; REMOVAL; ATR;
D O I
10.1007/s11244-007-0233-8
中图分类号
O69 [应用化学];
学科分类号
070301 [无机化学];
摘要
The CO preferential oxidation (CO-PROX) process can lead to a reduction of the CO concentration in the hydrogen-rich gas from WGS process of hydrocarbons reformate down to at least 10 ppmv or below, so as to enable its direct feeding to standard PEM fuel cells. Rh-based catalysts supported on 3A zeolite, alumina, titania or ceria were prepared and tested for potential application in CO-PROX operating in a temperature range compatible with PEM FCs (80-100 degrees C). Among the prepared catalysts, 1% Rh-3A zeolite catalyst was found to be the most suitable one for the CO-PROX at low temperature: it reduced the inlet CO concentration below 10 ppmv within a temperature range of at least 80-120 degrees C without the appearance of undesirable side reactions. In order to improve the oxygen selectivity toward the CO complete oxidation with a lowest as possible hydrogen parasitic oxidation, the oxygen amount in the feed gas composition was decreased. With 1% Rh-3A zeolite catalyst the lowest O-2 feed concentration was found to be 3 times the corresponding value of the CO stoichiometric oxidation (lambda = 2O(2)/CO = 3). Finally, with the goal to reduce the noble metal costs, tests at lower Rh load (from 1 to 0.5%) were carried out. No significant variations in both activity and width of complete CO conversion temperature range resulted for 0.5% Rh-3A catalyst. Therefore, this catalyst operating at lambda = 3 could potentially be used for the CO-PROX reaction at low temperature.
引用
收藏
页码:15 / 19
页数:5
相关论文
共 25 条
[1]
Estimation of the membrane methanol diffusion coefficient from open circuit voltage measurements in a direct methanol fuel cell [J].
Barragán, VM ;
Heinzel, A .
JOURNAL OF POWER SOURCES, 2002, 104 (01) :66-72
[2]
CO-free fuel processing for fuel cell applications [J].
Choudhary, TV ;
Goodman, DW .
CATALYSIS TODAY, 2002, 77 (1-2) :65-78
[3]
Diesel fuel processor for PEM fuel cells: Two possible altematives (ATR versus SR) [J].
Cutillo, A ;
Specchia, S ;
Antonini, M ;
Saracco, G ;
Specchia, V .
JOURNAL OF POWER SOURCES, 2006, 154 (02) :379-385
[4]
A compact CO selective oxidation reactor for solid polymer fuel cell powered vehicle application [J].
Dudfield, CD ;
Chen, R ;
Adcock, PL .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :214-222
[5]
*EU PROJ BIOF, ENK5CT200200612
[6]
*EU PROJ HYTR, TIPCT2003502577
[7]
*EU PROJ MIN, NNE5200100056
[8]
*EU PROJ PROF, NNE5199900434
[9]
CO removal from realistic methanol reformate via preferential oxidation -: performance of a Rh/MgO catalyst and comparison to Ru/γ-Al2O3, and Pt/-γ-Al2O3 [J].
Han, YF ;
Kahlich, MJ ;
Kinne, M ;
Behm, RJ .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 50 (04) :209-218
[10]
Kinetic study of selective CO oxidation in H2-rich gas on a Ru/γ-Al2O3 catalyst [J].
Han, YF ;
Kahlich, MJ ;
Kinne, M ;
Behm, RJ .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2002, 4 (02) :389-397