Study of the performance of Rh/La2O3-SiO2 and Rh/CeO2 catalysts for SR of ethanol in a conventional fixed-bed reactor and a membrane reactor

被引:21
作者
da Silva, Adriana M. [1 ]
Mattos, Lisiane V. [2 ]
Munera, John [3 ]
Lombardo, Eduardo [2 ]
Noronha, Fabio B. [1 ]
Cornaglia, Laura [3 ]
机构
[1] Inst Nacl Tecnol, BR-20081312 Rio De Janeiro, Brazil
[2] Univ Fed Fluminense, BR-24210240 Niteroi, RJ, Brazil
[3] INCAPE FIQ UNL CONICET, Inst Invest Catalisis & Petroquim, RA-3000 Santa Fe, Argentina
关键词
Ethanol steam reforming; Rh-based catalysts; Membrane reactor; STEAM REFORMING REACTION; HYDROGEN-PRODUCTION; REACTION-MECHANISM; PD; PRESSURE; OXIDATION; TEMPERATURE; METHANE;
D O I
10.1016/j.ijhydene.2015.01.106
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
The performance of Rh/La2O3-SiO2 and Rh/CeO2 catalysts for steam reforming of ethanol was investigated in a conventional fixed-bed reactor and a membrane reactor. This reactor was built with a self-supported Pd-Ag membrane, and its performance was compared to that the conventional reactor employing the same residence time and temperature. The effect of steam to ethanol molar ratio, ethanol concentration, temperature and contact time over hydrogen permeation and hydrogen recovery was investigated. In all cases, the ethanol conversion was kept at 100%, and the products formed were only H-2, CO2, CO and CH4. In the membrane reactor, the overall ethanol reforming reaction was favored without the formation of carbon deposits. The highest permeated and H-2 recovery was obtained for low ethanol content in the feed (high H2O/Ethanol ratio) and the methane formation was unfavored, in agreement with the high production of hydrogen. A slight difference in the hydrogen permeated/feed ethanol ratio was observed at higher sweep gas flow rates being higher for Rh supported on CeO2 in comparison with the Rh/La2O3-SiO2 catalyst. The best results were obtained with a H2O/Ethanol molar ratio equal to 10 and the highest membrane permeation area. Under these conditions, the H-2 recovery reached values of about 70% and the hydrogen produced for each mole of ethanol exhibited the highest value close to 2.8. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4154 / 4166
页数:13
相关论文
共 40 条
[31]   Hydrogen production from bio-ethanol steam reforming reaction in a Pd/PSS membrane reactor [J].
Seelam, Prem K. ;
Liguori, Simona ;
Iulianelli, Adolfo ;
Pinacci, Pietro ;
Calabro, Vincenza ;
Huuhtanen, Mika ;
Keiski, Riitta ;
Piemonte, Vincenzo ;
Tosti, Silvano ;
De Falco, Marcello ;
Basile, Angelo .
CATALYSIS TODAY, 2012, 193 (01) :42-48
[32]   SURFACE CHARACTERIZATION OF ALUMINA-SUPPORTED CERIA [J].
SHYU, JZ ;
WEBER, WH ;
GANDHI, HS .
JOURNAL OF PHYSICAL CHEMISTRY, 1988, 92 (17) :4964-4970
[33]   Hydrogen production through CO2 reforming of CH4 over Pt/CeZrO2/Al2O3 catalysts using a Pd-Ag membrane reactor [J].
Silva, Fabiano A. ;
Hori, Carla E. ;
da Silva, Adriana M. ;
Mattos, Lisiane V. ;
Munera, John ;
Cornaglia, Laura ;
Noronha, Fabio B. ;
Lombardo, Eduardo .
CATALYSIS TODAY, 2012, 193 (01) :64-73
[34]  
Song H, 2010, J PHYS CHEM A, V114, P3796, DOI [10.1021/jp905608c, 10.1021/jp905608e]
[35]   Low temperature ethanol steam reforming in a Pd-Ag membrane reactor - Part 1: Ru-based catalyst [J].
Tosti, S. ;
Basile, A. ;
Borgognoni, F. ;
Capaldo, V. ;
Cordiner, S. ;
Di Cave, S. ;
Gallucci, F. ;
Rizzello, C. ;
Santucci, A. ;
Traversa, E. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 308 (1-2) :250-257
[36]   Pd-based membrane reactors for producing ultra pure hydrogen: Oxidative reforming of bio-ethanol [J].
Tosti, S. ;
Zerbo, M. ;
Basile, A. ;
Calabro, V. ;
Borgognoni, F. ;
Santucci, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (01) :701-707
[37]   Pressure effect in ethanol steam reforming via dense Pd-based membranes [J].
Tosti, Silvano ;
Fabbricino, Massimiliano ;
Moriani, Andrea ;
Agatiello, Giuseppe ;
Scudieri, Carmela ;
Borgognoni, Fabio ;
Santucci, Alessia .
JOURNAL OF MEMBRANE SCIENCE, 2011, 377 (1-2) :65-74
[38]   Ethanol steam reforming kinetics of a Pd-Ag membrane reactor [J].
Tosti, Silvano ;
Basile, Angelo ;
Borelli, Rodolfo ;
Borgognoni, Fabio ;
Castelli, Stefano ;
Fabbricino, Massimiliano ;
Gallucci, Fausto ;
Licusati, Celeste .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (11) :4747-4754
[39]   Experimental and kinetic studies of the ethanol steam reforming reaction equipped with ultrathin Pd and Pd-Cu membranes for improved conversion and hydrogen yield [J].
Yun, Samhun ;
Lim, Hankwon ;
Oyama, S. Ted .
JOURNAL OF MEMBRANE SCIENCE, 2012, 409 :222-231
[40]   X-ray photoelectron spectroscopy study of rhodium particle growth on different alumina surfaces [J].
Zafeiratos, S ;
Nehasil, V ;
Ladas, S .
SURFACE SCIENCE, 1999, 433 :612-616