Low temperature ethanol steam reforming for process intensification: New Ni/MxO-ZrO2 active and stable catalysts prepared by flame spray pyrolysis

被引:27
作者
Compagnoni, Matteo [1 ,2 ]
Tripodi, Antonio [1 ,2 ]
Di Michele, Alessandro [3 ]
Sassi, Paola [4 ]
Signoretto, Michela [5 ]
Rossetti, Ilenia [1 ,2 ]
机构
[1] Univ Milan, Dip Chim, INSTM Unit, Chem Plants & Ind Chem Grp, Via C Golgi 19, I-20133 Milan, Italy
[2] CNR, ISTM, I-20133 Milan, Italy
[3] Univ Perugia, Dip Fis & Geol, Via Pascoli, Perugia, Italy
[4] Univ Perugia, Dip Chim Biol & Biotecnol, Via Elce Sotto 8, Perugia, Italy
[5] Ca Foscari Univ, Mol Sci & Nanosyst Dept, CatMat Lab, INSTM Unit, Campus Sci,Via Torino 155, I-30172 Venice, VE, Italy
关键词
Low temperature ethanol steam reforming; Coke formation; Flame spray pyrolysis; Alkali doping; Ni-based catalysts; Catalyst deactivation; ALKALINE-EARTH METALS; HYDROGEN-PRODUCTION; PROCESS SIMULATION; NI/ZRO2; CATALYSTS; AMMONIA-SYNTHESIS; SYNGAS PRODUCTION; COKE FORMATION; BIO-ETHANOL; NANOPARTICLE SYNTHESIS; REACTION-MECHANISM;
D O I
10.1016/j.ijhydene.2017.09.123
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
Steam reforming of hydrocarbons is a mature technology and its implementation on other substrates such as bio-ethanol appears as a ready opportunity to produce H-2 from renewable sources. The Low Temperature Ethanol Steam Reforming (LT-ESR, 300-500 degrees C) could be a really efficient technology from the energetic point of view. However, deactivation by coke deposition remains the biggest issue, due to inefficient carbon gasification by steam in such low temperature range. We demonstrated the feasibility of the process at low temperature taking into account both activity and deactivation issues. The attention was focused on the addition of basic promoters and on the development of an unconventional preparation procedure, in comparison with a traditional precipitation/impregnation route, to improve stability and activity. Therefore, in this work several catalysts were studied, differently promoted by alkali and alkali earth oxides (CaO, MgO, K2O) using a non conventional doping method. H-2 yield and selectivity to CO demonstrated tightly relatedto the promoter adopted. Flame Spray Pyrolysis synthesis of nickel nanoparticles stabilized in a zirconia matrix (Ni/MxO-ZrO2) was performed, obtaining more stable catalysts toward deactivation by coking with respect to the analogous prepared by traditional precipitation/impregnation. The effect of the doping using a scalable one -pot technique was investigated by means of characterization of fresh catalysts and activity testing. Catalyst resistance toward deactivation was studied by SEM-EDX, TEM, Raman spectroscopy and temperature programmed analysis. Among the promoters, CaO and K2O showed the best performance, producing a reformate with low CO/CO2 ratio and, thus, leading to higher H-2 yield with consequent lower impact on H-2 purification in an integrated process. K2O deeply modified the chemical behaviour of the catalyst allowing to achieve a significant H-2 production also at very low temperature (300 degrees C). (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:28193 / 28213
页数:21
相关论文
共 95 条
[1]   Catalyst development for steam reforming of methane and model biogas at low temperature [J].
Angeli, Sofia D. ;
Turchetti, Luca ;
Monteleone, Giulia ;
Lemonidou, Angeliki A. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2016, 181 :34-46
[2]  
[Anonymous], 2014, CRC Handbook of Chemistry and Physics, V95th, P3
[3]  
[Anonymous], 2015, PROGR CLEAN ENERGY, DOI DOI 10.1007/978-3-319-16709-1_51
[4]   Synthesis of NiO-MgO-ZrO2 catalysts and their performance in reforming of model biogas [J].
Asencios, Yvan J. O. ;
Bellido, Jorge D. A. ;
Assaf, Elisabete M. .
APPLIED CATALYSIS A-GENERAL, 2011, 397 (1-2) :138-144
[5]   Nickel catalysts supported on ZrO2, Y2O3-stabilized ZrO2 and CaO-stabilized ZrO2 for the steam reforming of ethanol:: Effect of the support and nickel load [J].
Bellido, J. D. A. ;
Assaf, E. M. .
JOURNAL OF POWER SOURCES, 2008, 177 (01) :24-32
[6]   Effect of adding CaO to ZrO2 support on nickel catalyst activity in dry reforming of methane [J].
Bellido, Jorge D. A. ;
De Souza, Jose E. ;
M'Peko, Jean-Claude ;
Assaf, Elisabete M. .
APPLIED CATALYSIS A-GENERAL, 2009, 358 (02) :215-223
[7]   New low-temperature preparations of some simple and mixed Co and Ni dispersed sulfides and their chemical behavior in reducing atmosphere [J].
Bezverkhyy, I ;
Danot, M ;
Afanasiev, P .
INORGANIC CHEMISTRY, 2003, 42 (05) :1764-1768
[8]   The effect of impurities on the steam reforming of ethanol over ruthenium/alumina [J].
Bilal, Muhammad ;
Jackson, S. David .
CATALYSIS SCIENCE & TECHNOLOGY, 2014, 4 (11) :4055-4064
[9]   Effect of Ba and K addition and controlled spatial deposition of Rh in Rh/Al2O3 catalysts for CO2 hydrogenation [J].
Buechel, Robert ;
Baiker, Alfons ;
Pratsinis, Sotiris E. .
APPLIED CATALYSIS A-GENERAL, 2014, 477 :93-101
[10]   Hydrogen from alcohols: IR and flow reactor studies [J].
Busca, Guido ;
Montanari, Tania ;
Resini, Carlo ;
Ramis, Gianguido ;
Costantino, Umberto .
CATALYSIS TODAY, 2009, 143 (1-2) :2-8