TY - JOUR
T1 - Selective Hydrodeoxygenation of Guaiacol to Phenolics by Ni/Anatase TiO 2 Catalyst Formed by Cross-Surface Migration of Ni and TiO 2
AU - Zhang, Xiaoqiang
AU - Yan, Peifang
AU - Zhao, Bin
AU - Liu, Kairui
AU - Kung, Mayfair C.
AU - Kung, Harold H.
AU - Chen, Shanyong
AU - Zhang, Z. Conrad
N1 - Funding Information:
This work was supported by the “Global Expert” program of China and National Natural Science Foundation of China (Grants 21690084 and 21721004). H.H.K. and M.C.K acknowledge support from the U.S. Department of Energy (Grant DE-FG02-03ER15457). The authors are grateful to CAS/SAFEA International Partnership Program for Creative Research Teams. Dedicated to the 70th anniversary of Dalian Institute of Chemical Physics, CAS.
Publisher Copyright:
© Copyright 2019 American Chemical Society.
PY - 2019/4/5
Y1 - 2019/4/5
N2 - The catalytic properties of physical mixtures of Ni particles (100-200 nm) with nanoparticles of anatase TiO 2 (TiO 2 -A), ZrO 2 , Al 2 O 3 , rutile TiO 2 (TiO 2 -R), and CeO 2 were investigated for the hydrodeoxygenation (HDO) of guaiacol. High selectivities to phenolics were obtained only for Ni mixed with anatase TiO 2 (Ni and TiO 2 -A), while saturated hydrocarbons were the main products for the mixtures with other supports. By thermal treatment in hydrogen gas only at 300 °C or higher and subsequently separating the large Ni particles from the TiO 2 -A particles with a magnet, it was further discovered that there was migration of TiO 2 from TiO 2 -A onto the large Ni particles, resulting in an amorphous TiO 2 overlayer on the Ni particles as evidenced by high-resolution TEM, and vice versa, migration of Ni onto TiO 2 -A. The TiO 2 overlayer rendered the Ni particles completely inactive as a hydrogenation/hydrodeoxygenation catalyst. Conversely, the small amounts of Ni (<1.5 wt %) migrated onto TiO 2 -A formed highly dispersed Ni, undetectable by high-resolution TEM (<2 nm), that were remarkably highly active for HDO of guaiacol, producing selectively phenolics. Such highly selective HDO catalysts could also be formed by incipient wetness impregnation of Ni in loadings above 2 wt % onto the TiO 2 -A, but it was essential to pretreat the sample in H 2 at 300 °C or higher. Pretreatment in H 2 at 200 °C generated catalysts that produced saturated ring products. The activity of the impregnated catalysts, as measured by guaiacol conversion, increased linearly with Ni loading below 0.5 wt %. The activity continued to increase with Ni loading but more slowly up to 2 wt %, beyond which there was little further change. The results suggested that two types of Ni species existed on the TiO 2 -A surface. One type consisted of a cluster of Ni atoms that were dominant on larger Ni particles that were active in aromatic ring hydrogenation and hydrodeoxygenation. They were readily covered by reducible TiO 2 -A at 300 °C or higher due to the traditional strong metal support interaction (SMSI) effect and became inactive. Another type was clusters of a very small number of Ni atoms, perhaps one atom, that were present as highly dispersed Ni clusters interacting strongly with the defect sites of TiO 2 -A. The strong interaction of this type of Ni with the TiO 2 defect deterred TiO x migration allowing surface exposed Ni atoms to catalyze the HDO of guaiacol with very high selectivities that were not characteristic of typical Ni particles.
AB - The catalytic properties of physical mixtures of Ni particles (100-200 nm) with nanoparticles of anatase TiO 2 (TiO 2 -A), ZrO 2 , Al 2 O 3 , rutile TiO 2 (TiO 2 -R), and CeO 2 were investigated for the hydrodeoxygenation (HDO) of guaiacol. High selectivities to phenolics were obtained only for Ni mixed with anatase TiO 2 (Ni and TiO 2 -A), while saturated hydrocarbons were the main products for the mixtures with other supports. By thermal treatment in hydrogen gas only at 300 °C or higher and subsequently separating the large Ni particles from the TiO 2 -A particles with a magnet, it was further discovered that there was migration of TiO 2 from TiO 2 -A onto the large Ni particles, resulting in an amorphous TiO 2 overlayer on the Ni particles as evidenced by high-resolution TEM, and vice versa, migration of Ni onto TiO 2 -A. The TiO 2 overlayer rendered the Ni particles completely inactive as a hydrogenation/hydrodeoxygenation catalyst. Conversely, the small amounts of Ni (<1.5 wt %) migrated onto TiO 2 -A formed highly dispersed Ni, undetectable by high-resolution TEM (<2 nm), that were remarkably highly active for HDO of guaiacol, producing selectively phenolics. Such highly selective HDO catalysts could also be formed by incipient wetness impregnation of Ni in loadings above 2 wt % onto the TiO 2 -A, but it was essential to pretreat the sample in H 2 at 300 °C or higher. Pretreatment in H 2 at 200 °C generated catalysts that produced saturated ring products. The activity of the impregnated catalysts, as measured by guaiacol conversion, increased linearly with Ni loading below 0.5 wt %. The activity continued to increase with Ni loading but more slowly up to 2 wt %, beyond which there was little further change. The results suggested that two types of Ni species existed on the TiO 2 -A surface. One type consisted of a cluster of Ni atoms that were dominant on larger Ni particles that were active in aromatic ring hydrogenation and hydrodeoxygenation. They were readily covered by reducible TiO 2 -A at 300 °C or higher due to the traditional strong metal support interaction (SMSI) effect and became inactive. Another type was clusters of a very small number of Ni atoms, perhaps one atom, that were present as highly dispersed Ni clusters interacting strongly with the defect sites of TiO 2 -A. The strong interaction of this type of Ni with the TiO 2 defect deterred TiO x migration allowing surface exposed Ni atoms to catalyze the HDO of guaiacol with very high selectivities that were not characteristic of typical Ni particles.
KW - SMSI or strong metal-support interaction
KW - guaiacol hydrodeoxygenation
KW - lignin
KW - phenol
KW - titania and nickel
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U2 - 10.1021/acscatal.9b00400
DO - 10.1021/acscatal.9b00400
M3 - Article
AN - SCOPUS:85063385125
SN - 2155-5435
VL - 9
SP - 3551
EP - 3563
JO - ACS Catalysis
JF - ACS Catalysis
IS - 4
ER -