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author:

Yang, Lei (Yang, Lei.) [1] | Cao, Hong (Cao, Hong.) [2] | Yue, Yuanyuan (Yue, Yuanyuan.) [3] | Yang, Chen (Yang, Chen.) [4] | Liu, Haiyan (Liu, Haiyan.) [5] | Wang, Tinghai (Wang, Tinghai.) [6] | Bao, Xiaojun (Bao, Xiaojun.) [7]

Indexed by:

EI

Abstract:

Aiming at the rational design and controllable preparation of highly selective fluid catalytic cracking (FCC) naphtha hydrodesulfurization (HDS) catalyst, a two-dimensional lattice Boltzmann method with multi-relaxation-time collision operator was developed to simulate the intraparticle diffusivities in alumina supports. The simulation results showed that, in a series of virtual alumina supports with the identical mesoporous structure but different macroporous structures, which were constructed via the random generation of macro-mesopores, the intraparticle diffusivity increases sharply with the increasing macropore volume and diameter, with the one having macropore volume 0.55 cm3/g and macropore diameter 500 nm simultaneously guaranteeing both satisfactory intraparticle diffusion performance and suitable crushing strength. Based on the simulation results, five γ-Al2O3 supports with the identical mesoporous structure but different macroporous structures were synthesized from the same pseudo-boehmite precursor by using sodium polyacrylate and different amounts of water during shaping, from which five CoMo/γ-Al2O3 catalysts were prepared. The HDS assessment results obtained using a real FCC naphtha showed that, compared with the reference catalyst prepared from an alumina without macropores, the catalysts prepared from the aluminas with different macroporous structures displayed higher HDS selectivity due to the enhanced diffusion in macropores. The systematic characterization results demonstrated that the enhanced HDS activities and selectivities of the macroporous alumina supported catalysts are mainly attributed to the enhanced diffusion in macropores. © 2020 Elsevier B.V.

Keyword:

Alumina Aluminum oxide Catalyst selectivity Catalyst supports Corundum Diffusion Fluid catalytic cracking Hydrodesulfurization Naphthas Structural design

Community:

  • [ 1 ] [Yang, Lei]State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing; 102249, China
  • [ 2 ] [Cao, Hong]National Engineering Research Center of Chemical Fertilizer, College of Chemical Engineering, Fuzhou University, Fuzhou; 350116, China
  • [ 3 ] [Yue, Yuanyuan]National Engineering Research Center of Chemical Fertilizer, College of Chemical Engineering, Fuzhou University, Fuzhou; 350116, China
  • [ 4 ] [Yang, Chen]National Engineering Research Center of Chemical Fertilizer, College of Chemical Engineering, Fuzhou University, Fuzhou; 350116, China
  • [ 5 ] [Liu, Haiyan]State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing; 102249, China
  • [ 6 ] [Wang, Tinghai]National Engineering Research Center of Chemical Fertilizer, College of Chemical Engineering, Fuzhou University, Fuzhou; 350116, China
  • [ 7 ] [Bao, Xiaojun]State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing; 102249, China

Reprint 's Address:

  • [wang, tinghai]national engineering research center of chemical fertilizer, college of chemical engineering, fuzhou university, fuzhou; 350116, china

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Source :

Fuel Processing Technology

ISSN: 0378-3820

Year: 2020

Volume: 208

7 . 0 3 3

JCR@2020

7 . 2 0 0

JCR@2023

ESI HC Threshold:160

JCR Journal Grade:1

CAS Journal Grade:2

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count: 12

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 1

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