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
[11]   Effective and stable bioethanol steam reforming catalyst based on Ni and Co supported on all-silica delaminated ITQ-2 zeolite [J].
Chica, Antonio ;
Sayas, Salvador .
CATALYSIS TODAY, 2009, 146 (1-2) :37-43
[12]  
Cullity B.D., 1956, Elements of X-ray Diffraction, P261
[13]   Catalysts based on Co-Birnessite and Co-Todorokite for the efficient production of hydrogen by ethanol steam reforming [J].
Da Costa-Serra, J. F. ;
Chica, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (35) :16859-16865
[14]   Bioethanol steam reforming on Co/ITQ-18 catalyst: Effect of the crystalline structure of the delaminated zeolite ITQ-18 [J].
Da Costa-Serra, J. F. ;
Chica, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (06) :3862-3869
[15]   Co/ZnO and Ni/ZnO catalysts for hydrogen production by bioethanol steam reforming. Influence of ZnO support morphology on the catalytic properties of Co and Ni active phases [J].
Da Costa-Serra, J. F. ;
Guil-Lopez, R. ;
Chica, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (13) :6709-6716
[16]  
Dashtban M, 2012, J-FOR, V2, P44
[17]   Evaluation of the performance of Ni/La2O3 catalyst prepared from LaNiO3 perovskite-type oxides for the production of hydrogen through steam reforming and oxidative steam reforming of ethanol [J].
de Lima, Sania M. ;
da Silva, Adriana M. ;
da Costa, Lidia O. O. ;
Assaf, Jose M. ;
Jacobs, Gary ;
Davis, Burtron H. ;
Mattos, Lisiane V. ;
Noronha, Fabio B. .
APPLIED CATALYSIS A-GENERAL, 2010, 377 (1-2) :181-190
[18]   Steam reforming of ethanol over Ni/MgAl2O4 catalysts [J].
Di Michele, Alessandro ;
Dell'Angelo, Anna ;
Tripodi, Antonio ;
Bahadori, Elnaz ;
Sanchez, Felipe ;
Motta, Davide ;
Dimitratos, Nikolaos ;
Rossetti, Ilenia ;
Ramis, Gianguido .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (02) :952-964
[19]   Hydrogen production by sorption-enhanced chemical looping steam reforming of ethanol in an alternating fixed-bed reactor: Sorbent to catalyst ratio dependencies [J].
Dou, Binlin ;
Zhang, Hua ;
Cui, Guomin ;
Wang, Zilong ;
Jiang, Bo ;
Wang, Kaiqiang ;
Chen, Haisheng ;
Xu, Yujie .
ENERGY CONVERSION AND MANAGEMENT, 2018, 155 :243-252
[20]   Study of Ni/CeO2-ZnO catalysts in the production of H2 from acetone steam reforming [J].
Elias, K. F. M. ;
Bednarczuk, L. ;
Assaf, E. M. ;
Ramirez de la Piscina, P. ;
Homs, N. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (25) :12628-12635