Kinetic and FTIR studies of 2-methyltetrahydrofuran hydrodeoxygenation on Ni2P/SiO2

被引:59
作者
Cho, Ara [1 ,2 ]
Kim, Hosoo [2 ]
Iino, Ayako [1 ]
Takagaki, Atsushi [1 ]
Oyama, S. Ted [1 ,3 ]
机构
[1] Univ Tokyo, Dept Chem Syst Engn, Bunkyo Ku, Tokyo 1138656, Japan
[2] Corp R&D, Taejon 305738, South Korea
[3] Virginia Tech, Dept Chem Engn, Blacksburg, VA 24061 USA
基金
美国国家科学基金会;
关键词
Hydrodeoxygenation; 2-Methyltetrahydrofuran; Ni2P/SiO2; Rake mechanism; In situ FTIR; NICKEL PHOSPHIDE CATALYSTS; METAL PHOSPHIDES; MODEL-COMPOUND; CO ADSORPTION; NI2P CATALYST; ACTIVE PHASE; BIOMASS; CONVERSION; PYROLYSIS; GUAIACOL;
D O I
10.1016/j.jcat.2014.07.021
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
The hydrodeoxygenation of 2-methyltetrahydrofuran (2-MTHF) at a medium pressure of 0.5 MPa is studied over a Ni2P/SiO2 catalyst. Contact time studies show the formation of n-pentanal, 1-pentanol, 2-pentanone, 2-pentanol, and 2-pentene, as reaction intermediates and the production of pentane and butane as major products. The results are consistent with adsorption of 2-MTHF followed by rate-determining ring-opening to form either 1-pentoxide or 2-pentoxide alkoxide intermediates. Subsequent hydrogen-transfer steps produce the various intermediates, a decarbonylation step of the pentanal forms n-butane and CO, and further hydrodeoxygenation steps result in n-pentane. Fitting of the results using a rake mechanism that considers adsorbed intermediates gives excellent agreement with experimental data, and agrees with a simulation with a simpler first-order model. The more detailed rake analysis indicates that the surface species from the 1-pentoxide intermediate are ten-fold more plentiful than those produced from the 2-pentoxide intermediate. In situ infrared measurements support this reaction mechanism. (C) 2014 Elsevier Inc. All rights reserved.
引用
收藏
页码:151 / 161
页数:11
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