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author:

Yun, G.-N. (Yun, G.-N..) [1] | Tyrone, Ghampson, I. (Tyrone, Ghampson, I..) [2] | Movick, W.J. (Movick, W.J..) [3] | Vargheese, V. (Vargheese, V..) [4] | Kobayashi, Y. (Kobayashi, Y..) [5] | Ted, Oyama, S. (Ted, Oyama, S..) [6]

Indexed by:

Scopus

Abstract:

Contact-time measurements based on sites are used to investigate the reaction sequence of the hydrodeoxygenation of γ-valerolactone (GVL) on Ni2P/MCM-41. The study is carried out at 300 °C and 0.5 MPa with site times of 0.29–6.1 s. A reaction network is proposed in which pentanoic acid and 2-methyltetrahydrofuran (2-MTHF) are formed in parallel initially and pentanal, butane and pentane are formed subsequently. A first-rank Delplot analysis (selectivity) gives a good fit, but higher-rank Delplots do not. The lack of applicability is explained by the magnitude of the rate constants, in which the rate constant for one of the later steps (the consumption of pentanal) is substantially larger than those for the preceding steps. For this reason, pentanal demonstrated the characteristics of a primary product and consequently affected the discrimination of higher rank products. A simulation of a model sequence with assumed rate constants confirms the reason why the Delplot method does not work for this reaction. Since the rate constants cannot be determined a priori to be of close magnitude, the Delplot method cannot be generally used to ascertain reaction sequences. © 2020 Elsevier Ltd

Keyword:

Conctact time analysis; Delplot analysis; Hydrodeoxygenation; Ni2P; Site-time; γ-valerolactone

Community:

  • [ 1 ] [Yun, G.-N.]Department of Chemical Engineering, Virginia Tech, Blacksburg, VA 24061, United States
  • [ 2 ] [Yun, G.-N.]Green Carbon Catalysis Research Center, Korea Research Institute of Chemical Technology (KRICT), 141 Gajeong-ro, Yuseong-gu, Daejeon, 34114, South Korea
  • [ 3 ] [Tyrone Ghampson, I.]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku, Tokyo, 113-8656, Japan
  • [ 4 ] [Movick, W.J.]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku, Tokyo, 113-8656, Japan
  • [ 5 ] [Vargheese, V.]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku, Tokyo, 113-8656, Japan
  • [ 6 ] [Kobayashi, Y.]Interdisciplinary Research Center for Catalytic Chemistry, National Institute of Advanced Industrial Science and Technology (AIST), Central 5, Higashi 1-1-1, Tsukuba, Ibaraki, 305-8565, Japan
  • [ 7 ] [Ted Oyama, S.]School of Chemical Engineering, Fuzhou University, Fuzhou, 350116, China
  • [ 8 ] [Ted Oyama, S.]Department of Chemical Systems Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku, Tokyo, 113-8656, Japan
  • [ 9 ] [Ted Oyama, S.]Department of Chemical Engineering, Virginia Tech, Blacksburg, VA 24061, United States

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Source :

Chemical Engineering Science

ISSN: 0009-2509

Year: 2020

Volume: 223

4 . 3 1 1

JCR@2020

4 . 1 0 0

JCR@2023

ESI HC Threshold:160

JCR Journal Grade:2

CAS Journal Grade:3

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count: 9

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 0

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