Published September 2021 | Version v1
Journal article

Combined DFT and microkinetic modeling study of S O 2 hydrodesulfurization reaction on N i 5 P 4 catalyst

  • 1. Center for Catalysis and Separations (CeCaS), Khalifa University, PO Box 127788, Abu Dhabi (United Arab Emirates)
  • 2. Department of Physics, Khalifa University of Science and Technology, PO BOX 127788, Abu Dhabi (United Arab Emirates)
  • 3. Department of Chemical Engineering, Khalifa University, PO BOX 127788, Abu Dhabi (United Arab Emirates)
  • 4. Department of Mechanical Engineering, Khalifa University, PO Box 127788, Abu Dhabi (United Arab Emirates)

Description

Highlights: • SO2 and H2 adsorptions were examined on low-index facets of Ni5P4using DFT. • Microkinetic model was developed for SO2 HDS over Ni5P4(0 0 1) surface. • The kinetic barriers of products formation influence selectivities. • H2S formation and desorption were found to be the rate-determining steps. Optimizing catalysts for the SO2 hydrodesulfurization (HDS) is a crucial step toward conforming with the environmental requirements concerning SO2 emissions. Nickel phosphides have been reported as efficient catalysts in HDS reaction. However, how HDS reaction proceeds on nickel phosphides is not well understood. On this context, the present work focuses on the mechanistic understanding of SO2 HDS reaction over Ni5P4surfaces. The adsorption of both reactants, SO2 and H2 molecules, on low-index facets of Ni5P4 crystal, namely (0 0 1), (0 1 1), (1 1 1), (1 1 0) , (1 0 1), (0 1 0) and (1 0 0) surfaces, were investigated using density functional theory (DFT) calculations. The stability of Ni5P4 surfaces was examined and (0 0 1) surface was found to be the most stable surface. Therefore, microkinetic modeling was conducted on Ni5P4(0 0 1) surface to predict the catalytic preferred pathways. Reaction towards H2S, main product, exhibited 100% selectivity at reaction temperatures below 700 K, however the selectivity towards H2O became dominant at higher temperatures. This is because the barrier for HS- hydrogenation to H2S (1.20 eV) is lower than that of the OH hydrogenation to H2O (2.37 eV). The model revealed that conversion of HS- ions to H2S was the rate-controlling step at reaction temperature below 500 K, whereas H2S desorption dominates the overall reaction rate at higher temperatures. The apparent activation energy of HDS reaction decreased considerably from 195 to 48 kJ/mol at reaction temperature range of 400–800 K. The reaction orders in SO2 and H2 increased with rising temperature, reaching 0.15 and 1.0, respectively, at 800 K.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.apsusc.2021.149872

Additional details

Identifiers

DOI
10.1016/j.apsusc.2021.149872;
PII
S016943322100948X;

Publishing Information

Journal Title
Applied Surface Science
Journal Volume
559
Journal Page Range
vp.
ISSN
0169-4332
CODEN
ASUSEE

Optional Information

Copyright
Copyright (c) 2021 Elsevier B.V. All rights reserved.