Sustainable production of hydrogen via steam reforming of furfural (SRF) with Co-catalyst supported on sepiolite

被引:12
作者
Sayas, S. [1 ]
Da Costa-Serra, J. F. [1 ]
Chica, A. [1 ]
机构
[1] Univ Politecn Valencia, Consejo Super Invest Cient, Inst Tecnol Quim, Avd De Los Naranjos S-N, Valencia 46022, Spain
关键词
Steam reforming; Cobalt catalyst; Natural sepiolite; Hydrogen production; Furfural; COBALT CATALYSTS; BIO-OIL; EFFICIENT PRODUCTION; MODEL COMPOUNDS; SYNTHESIS PARAMETERS; CU-NI; ETHANOL; CO; BIOETHANOL; CARBON;
D O I
10.1016/j.ijhydene.2020.04.185
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
Natural sepiolite is a mineral very abundant in Spain, being the main producer worldwide. This material is presented by the first time as promised support to prepare cobalt catalysts with high activity and hydrogen selectivity in the steam reforming of furfural (SRF). Two methods for cobalt incorporation on natural sepiolite, precipitation (PP) and incipient wetness impregnation (IWI), are explored and their influence in the preparation of catalysts highly active and selective in the SRF is studied. PP method makes possible to synthesize a catalytic material with high catalytic performance (high conversion of furfural, > 95%, and high hydrogen selectivity, 70%). Furthermore the production of non-desired byproducts such as CO, CH4 and acetone, decrease significantly in the catalyst prepared by PP (CoSep). Characterization by N-2 adsorption-desorption to determine surface area, XRD, TPR and TEM shows that PP method favors the formation of smaller metallic particles of Co with a high dispersion. These differential physicochemical properties seem to explain the better catalytic performance exhibited by the sepiolitic catalyst prepared by the PP method (CoSep). In addition, this catalyst exhibits also a higher resistance to deactivation after 24 h of reaction time. This fact seems to be related to the lower coke deposition on the catalyst prepared by precipitation and particularly, with the lower sinterization of the metallic Co particles during the steam reforming of furfural. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:17481 / 17489
页数:9
相关论文
共 67 条
[1]   Rh promoted and ZrO2/Al2O3 supported Ni/Co based catalysts: High activity for CO2 reforming, steam-CO2 reforming and oxy-CO2 reforming of CH4 [J].
Al-Fatesh, Ahmed ;
Singh, Sunit Kumar ;
Kanade, G. S. ;
Atia, Hanan ;
Fakeeha, Anis H. ;
Ibrahim, Ahmed A. ;
El-Toni, Ahmed Mohamed ;
Labhasetwar, Nitin K. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (27) :12069-12080
[2]   Steam reforming of different biomass tar model compounds over Ni/Al2O3 catalysts [J].
Artetxe, Maite ;
Alvarez, Jon ;
Nahil, Mohamad A. ;
Olazar, Martin ;
Williams, Paul T. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 136 :119-126
[3]   Recent progress in the development of catalysts for steam reforming of biomass tar model reaction [J].
Ashok, Jangam ;
Dewangan, Nikita ;
Das, Sonali ;
Hongmanorom, Plaifa ;
Wai, Ming Hui ;
Tomishige, Keiichi ;
Kawi, Sibudjing .
FUEL PROCESSING TECHNOLOGY, 2020, 199
[4]   Hydrogen production by ethanol reforming over NiZnAl catalysts [J].
Barroso, M. Noelia ;
Gomez, Manuel F. ;
Arrua, Luis A. ;
Abello, M. Cristina .
APPLIED CATALYSIS A-GENERAL, 2006, 304 (01) :116-123
[5]   High efficiency steam reforming of ethanol by cobalt-based catalysts [J].
Batista, MS ;
Santos, RKS ;
Assaf, EM ;
Assaf, JM ;
Ticianelli, EA .
JOURNAL OF POWER SOURCES, 2004, 134 (01) :27-32
[6]   Characterization of the activity and stability of supported cobalt catalysts for the steam reforming of ethanol [J].
Batista, MS ;
Santos, RKS ;
Assaf, EM ;
Assaf, JM ;
Ticianelli, EA .
JOURNAL OF POWER SOURCES, 2003, 124 (01) :99-103
[7]   Sustainable hydrogen production from bio-oil model compounds (meta-xylene) and mixtures (1-butanol, meta-xylene and furfural) [J].
Bizkarra, K. ;
Barrio, V. L. ;
Arias, P. L. ;
Cambra, J. F. .
BIORESOURCE TECHNOLOGY, 2016, 216 :287-293
[8]   Fischer-Tropsch synthesis over γ-calumina-supported cobalt catalysts:: Effect of support variables [J].
Borg, Oyvind ;
Erib, Sigrid ;
Blekkan, Edd A. ;
Storsaeter, Solvi ;
Wigum, Hanne ;
Rytter, Erling ;
Holmen, Anders .
JOURNAL OF CATALYSIS, 2007, 248 (01) :89-100
[9]   Co and La supported on Zn-Hydrotalcite-derived material as efficient catalyst for ethanol steam reforming [J].
Cerda-Moreno, C. ;
Da Costa-Serra, J. F. ;
Chico, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (25) :12685-12692
[10]   Direct reduction of nickel catalyst with model bio-compounds [J].
Cheng, Feng ;
Dupont, Valerie ;
Twigg, Martyn V. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2017, 200 :121-132