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author:

Ted Oyama, S. (Ted Oyama, S..) [1] | Yun, Gwang-Nam (Yun, Gwang-Nam.) [2] | Ahn, So-Jin (Ahn, So-Jin.) [3] | Bando, Kyoko K. (Bando, Kyoko K..) [4] | Takagaki, Atsushi (Takagaki, Atsushi.) [5] | Kikuchi, Ryuji (Kikuchi, Ryuji.) [6]

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EI

Abstract:

The understanding of catalytic mechanisms is enhanced by the observation of surface intermediates at reaction conditions using spectroscopic techniques, but this is insufficient, as the observed species may not be involved in the reaction. This work describes a general method of analysis of hydrogenation or oxidation reactions which uses transient spectroscopic data to determine whether an adsorbed species is a reactive intermediate or a spectator on the surface. The assumptions and limitations of the method are summarized. Although the technique is approximate, it is easy to implement, and provides order-of-magnitude estimates of the rate of reaction of an intermediate. The method consists of measuring the change of coverage of the species with time, dθ/dt, during adsorption in inert gas or at reaction conditions. An example is given with the hydrodeoxygenation of the model compound γ-valerolactone (GVL) using a Ni2P/MCM-41 catalyst, one of the most effective catalysts reported for the transformation. The reaction is relevant to the upgrading of bio-oil derived from pyrolysis of lignocellulosic feedstocks. The kinetics of the reaction and observation by in situ infrared spectroscopy of adsorbed GVL and its transformation to pentanoic acid are consistent with a Langmuir-Hinshelwood mechanism. Analysis by in situ transient X-ray absorption fine structure shows that the adsorbed GVL is a true reaction intermediate. © 2020 Elsevier Inc.

Keyword:

Catalysts Inert gases Infrared spectroscopy Reaction intermediates Reaction kinetics Spectroscopic analysis Surface reactions X ray absorption

Community:

  • [ 1 ] [Ted Oyama, S.]Fuzhou University, College of Chemical Engineering, Fuzhou; 350116, China
  • [ 2 ] [Ted Oyama, S.]Department of Chemical Engineering, Virginia Tech, Blacksburg; VA; 24061, United States
  • [ 3 ] [Ted Oyama, S.]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku; Tokyo; 113-8656, Japan
  • [ 4 ] [Yun, Gwang-Nam]Department of Chemical Engineering, Virginia Tech, Blacksburg; VA; 24061, United States
  • [ 5 ] [Yun, Gwang-Nam]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku; Tokyo; 113-8656, Japan
  • [ 6 ] [Yun, Gwang-Nam]Green Carbon Research Center, Korea Research Institute of Chemical Technology (KRICT), 141 Gajeong-ro, Yuseong-gu, Daejeon; 34114, Korea, Republic of
  • [ 7 ] [Ahn, So-Jin]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku; Tokyo; 113-8656, Japan
  • [ 8 ] [Bando, Kyoko K.]National Institute of Advanced Industrial Science and Technology, AIST Tsukuba Central 5, 1-1-1, Higashi, Tsukuba; Ibaraki; 305-8565, Japan
  • [ 9 ] [Takagaki, Atsushi]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku; Tokyo; 113-8656, Japan
  • [ 10 ] [Kikuchi, Ryuji]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku; Tokyo; 113-8656, Japan

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Source :

Journal of Catalysis

ISSN: 0021-9517

Year: 2021

Volume: 394

Page: 273-283

8 . 0 4 7

JCR@2021

6 . 5 0 0

JCR@2023

ESI HC Threshold:117

JCR Journal Grade:1

CAS Journal Grade:1

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count: 18

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 0

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