A mechanistic study on the decomposition of a model bio-oil compound for hydrogen production over a stepped Ni surface: Formic acid

被引:14
作者
Li, Xinbao [1 ]
Xuan, Kejie [1 ]
Zhu, Yingying [1 ]
Chen, Geng [1 ]
Yang, Guohua [1 ]
机构
[1] Ningbo Univ, Fac Maritime & Transportat, Ningbo 315211, Zhejiang, Peoples R China
基金
中国国家自然科学基金;
关键词
DFT; Bio-oil; Catalytic reforming; Formic acid; Hydrogen production; Ni catalyst; DENSITY-FUNCTIONAL THEORY; TOTAL-ENERGY CALCULATIONS; ELASTIC BAND METHOD; ACETIC-ACID; FAST PYROLYSIS; BIOMASS; DFT; CATALYSTS; METHANOL; OXIDATION;
D O I
10.1016/j.apsusc.2018.05.049
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
To obtain a clearer understanding of the catalytic bio-oil reforming mechanism, we performed density functional theory calculations on the decomposition of formic acid over a stepped Ni surface. Formic acid was selected as a model bio-oil compound. Fourteen elementary reactions were considered. All the zero-point-energy corrected activation energies and reaction energies were obtained. The kinetic parameters of the reaction rate constants and thermodynamic equilibrium constants in the temperature range of 300-1000 K were revealed. COOH formation and its subsequent dissociation are energetically easier than that of HCOO. When combined with kinetic modeling, the most preferable pathway for formic acid dissociation on the surface is HCOOH -> COOH -> CO. The rate-determining step is COOH dehydroxylation to CO, associating with an activation energy of 0.51 eV and a rate constant of 5.16 x 10(9) s(-1) at 773 K. In addition, HCOO will be slowly accumulated on the surface as the temperature rises. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:87 / 95
页数:9
相关论文
共 48 条
[41]   Biomass to hydrogen via fast pyrolysis and catalytic steam reforming of the pyrolysis oil or its fractions [J].
Wang, D ;
Czernik, S ;
Montane, D ;
Mann, M ;
Chornet, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1507-1518
[42]   Hydrogen production via catalytic reforming of the bio-oil model compounds: Acetic acid, phenol and hydroxyacetone [J].
Wang, Shurong ;
Cai, Qinjie ;
Zhang, Fan ;
Li, Xinbao ;
Zhang, Li ;
Luo, Zhongyang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (32) :18675-18687
[43]   Catalytic steam reforming of bio-oil model compounds for hydrogen production over coal ash supported Ni catalyst [J].
Wang, Shurong ;
Zhang, Fan ;
Cai, Qinjie ;
Li, Xinbao ;
Zhu, Lingjun ;
Wang, Qi ;
Luo, Zhongyang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (05) :2018-2025
[44]   Bio-oil catalytic reforming without steam addition: Application to hydrogen production and studies on its mechanism [J].
Wang, Shurong ;
Li, Xinbao ;
Zhang, Fan ;
Cai, Qinjie ;
Wang, Yurong ;
Luo, Zhongyang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (36) :16038-16047
[45]   Experimental research on acetic acid steam reforming over Co-Fe catalysts and subsequent density functional theory studies [J].
Wang, Shurong ;
Li, Xinbao ;
Guo, Long ;
Luo, Zhongyang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (15) :11122-11131
[46]   DIRECT PROOF OF THE HYDROGEN IN THE METHANOL ADSORBATE AT PLATINUM - AN ECTDMS STUDY [J].
WILHELM, S ;
VIELSTICH, W ;
BUSCHMANN, HW ;
IWASITA, T .
JOURNAL OF ELECTROANALYTICAL CHEMISTRY, 1987, 229 (1-2) :377-384
[47]   Theoretical Analysis of Transition-Metal Catalysts for Formic Acid Decomposition [J].
Yoo, Jong Suk ;
Abild-Pedersen, Frank ;
Norskov, Jens K. ;
Studt, Felix .
ACS CATALYSIS, 2014, 4 (04) :1226-1233
[48]   DFT studies of dry reforming of methane on Ni catalyst [J].
Zhu, Yi-An ;
Chen, De ;
Zhou, Xing-Gui ;
Yuan, Wei-Kang .
CATALYSIS TODAY, 2009, 148 (3-4) :260-267