Mechanistic insights into the catalytic elimination of tar and the promotional effect of boron on it: first-principles study using toluene as a model compound

被引:59
作者
Quang Thang Trinh [1 ]
Anh Vu Nguyen [2 ]
Dang Chinh Huynh [2 ]
Thanh Huyen Pham [2 ]
Mushrif, Samir H. [1 ]
机构
[1] Nanyang Technol Univ, Sch Chem & Biomed Engn, 62 Nanyang Dr, Singapore 637459, Singapore
[2] Hanoi Univ Sci & Technol, Sch Chem Engn, 1 Dai Co Viet St, Hanoi, Vietnam
关键词
NI-BASED CATALYSTS; FISCHER-TROPSCH CATALYSTS; DENSITY-FUNCTIONAL THEORY; BIOMASS GASIFICATION; HYDROGEN-PRODUCTION; SURFACE-CHEMISTRY; SELECTIVE HYDROGENATION; NI/OLIVINE CATALYST; 1ST PRINCIPLES; METAL-SURFACES;
D O I
10.1039/c6cy00358c
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
Tar is the undesired viscous black liquid produced during the gasification of biomass. Catalytic elimination of tar is feasible and is economically promising. In the present investigation, we performed first-principles calculations (i) to elucidate the decomposition mechanism of tar on the popular nickel (Ni) catalyst and (ii) to reveal the promotional effect of boron (B) in improving the activity and stability of the Ni catalyst for tar decomposition. Being the most abundant component of tar, toluene was chosen as a model compound. On the Ni(111) surface, toluene adsorbs strongly in a bridge configuration and the activation barrier for methyl C-H dissociation is 72 kJ mol(-1). Toluene can further decompose on the Ni(111) surface via stepwise dehydrogenation of the methyl group. The aromatic C-H bond at the ortho position could only be activated after the complete dehydrogenation of the methyl group, which is followed by subsequent ring opening (activation barriers are 112 and 84 kJ mol(-1), respectively) and C-C cleavages, to generate smaller hydrocarbons. The incorporation of subsurface B into the Ni catalyst (B-Ni) results in a corrugated Ni top surface and toluene adsorbs more strongly by 11 kJ mol(-1) on the B-Ni catalyst than on pure Ni. Although the mechanism of toluene decomposition remains unchanged after doping with boron, the decomposition of toluene is significantly promoted on B-Ni. The activation barrier for the first methyl C-H dissociation on B-Ni is reduced to 51 kJ mol(-1). Subsequent methyl C-H activations are also promoted on the B-Ni catalyst, but to a smaller extent. The aromatic C-H activation is also strongly promoted (89 kJ mol(-1) vs. 112 kJ mol(-1) on pure Ni). Additional calculations on stepped surface models of Ni show that the activation barriers of toluene decomposition on the B-Ni surface are very close to those on B5 and F4 step sites of pure Ni, thus suggesting that the promotional effect of B on the catalytic activity of Ni could be mainly attributed to the creation of step-like corrugations on the Ni surface. These corrugations could also inhibit the formation of graphene-like structures on B-Ni.
引用
收藏
页码:5871 / 5883
页数:13
相关论文
共 79 条
[2]   Review of catalysts for tar elimination in Biomass gasification processes [J].
Abu El-Rub, Z ;
Bramer, EA ;
Brem, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (22) :6911-6919
[3]   Biomass Oxidation: Formyl CH Bond Activation by the Surface Lattice Oxygen of Regenerative CuO Nanoleaves [J].
Amaniampong, Prince N. ;
Quang Thang Trinh ;
Wang, Bo ;
Borgna, Armando ;
Yang, Yanhui ;
Mushrif, Samir H. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2015, 54 (31) :8928-8933
[4]   Tar reduction in biomass producer gas via mechanical, catalytic and thermal methods: A review [J].
Anis, Samsudin ;
Zainal, Z. A. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2011, 15 (05) :2355-2377
[5]   Basic relationships in the pre-reforming of n-hexane on Ni/MgO catalyst [J].
Arena, Francesco .
AICHE JOURNAL, 2006, 52 (08) :2823-2831
[6]   Hydrogen production by steam reforming of n-butane over supported Ni and Pt-Ni catalysts [J].
Avci, AK ;
Trimm, DL ;
Aksoylu, AE ;
Önsan, ZI .
APPLIED CATALYSIS A-GENERAL, 2004, 258 (02) :235-240
[7]   Commercial steam reforming catalysts to improve biomass gasification with steam-oxygen mixtures. 2. Catalytic tar removal [J].
Aznar, MP ;
Caballero, MA ;
Gil, J ;
Martin, JA ;
Corella, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (07) :2668-2680
[8]   Origin of the Formation of Nanoislands on Cobalt Catalysts during Fischer-Tropsch Synthesis [J].
Banerjee, Arghya ;
van Bave, Alexander P. ;
Kuipers, Herman P. C. E. ;
Saeys, Mark .
ACS CATALYSIS, 2015, 5 (08) :4756-4760
[9]   Chemisorption of methane on Ni(100) and Ni(111) surfaces with preadsorbed potassium [J].
Bengaard, HS ;
Alstrup, I ;
Chorkendorff, I ;
Ullmann, S ;
Rostrup-Nielsen, JR ;
Norskov, JK .
JOURNAL OF CATALYSIS, 1999, 187 (01) :238-244
[10]   Design of a surface alloy catalyst for steam reforming [J].
Besenbacher, F ;
Chorkendorff, I ;
Clausen, BS ;
Hammer, B ;
Molenbroek, AM ;
Norskov, JK ;
Stensgaard, I .
SCIENCE, 1998, 279 (5358) :1913-1915