Shangfeng Du

Dr. Shangfeng Du

School of Chemical Engineering, University of Birmingham, Edgbaston, Birmingham B152TT, UK
orcid

Research Focus & Metrics

Academic Career Length

21Years (2006-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 June 2013 in Journal of Power Sources
Verified
Journal Article
Open access
ACAmrit Chandan
Amrit Chandan
MHMariska Hattenberger
Mariska Hattenberger
AEAhmad El-Kharouf
Ahmad El-Kharouf
SDShangfeng Du
Shangfeng Du
ADAman Dhir
Aman Dhir
WBWaldemar Bujalski
Waldemar Bujalski

1 December 2016 in Applied Catalysis B: Environment and Energy
Verified
Journal Article
Open access
YLYaxiang Lu
Yaxiang Lu
SDShangfeng Du
Shangfeng Du
Robert Steinberger-WilckensRobert Steinberger-Wilckens
Robert Steinberger-Wilckens

15 October 2015 in RSC Advances
Verified
Journal Article
Closed access
PDF file
YWYan Wang
Yan Wang
HGHongtao Guan
Hongtao Guan
SDShangfeng Du
Shangfeng Du
YWYude Wang
Yude Wang
MnO2 nanorod/reduced graphene oxide nanocomposites synthesized by a simple one-step hydrothermal method significantly improved the electromagnetic wave absorption performance and widened the effective absorption bandwidth.


3 February 2022 in Chemical Engineering Journal
Verified
Journal Article
Open access
SSShibo Shao
Shibo Shao
KWKe Wang
Ke Wang
JLJason B. Love
Jason B. Love
JYJialin Yu
Jialin Yu
SDShangfeng Du
Shangfeng Du
XFXianfeng Fan
Xianfeng Fan

1 February 2016 in Energy
Verified
Journal Article
Open access
LXLei Xing
Lei Xing
SDShangfeng Du
Shangfeng Du
Rui ChenRui Chen
Rui Chen
MMMohamed Mamlouk
Mohamed Mamlouk
KSKeith Scott
Keith Scott
This paper is in closed access until 7th Jan 2017.A two-dimensional along-the-channel CFD (computational fluid dynamic) model, coupled with a two-phase flow model of liquid water and gas transport for a PEM (proton exchange membrane) fuel cell is described. The model considers non-isothermal operation and thus the non-uniform temperature distribution in the cell structure. Water phase-transfer between the vapour, liquid water and dissolved phase is modelled with the combinational transport mechanism through the membrane. Liquid water saturation is simulated inside the electrodes and channels at both the anode and cathode sides. Three types of models are compared for the HOR (hydrogen oxidation reaction) and ORR (oxygen reduction reaction) in catalyst layers, including Butler–Volmer (B–V), liquid water saturation corrected B–V and agglomerate mechanisms. Temperature changes in MEA (membrane electrode assembly) and channels due to electrochemical reaction, ohmic resistance and water phase-transfer are analysed as a function of current density. Nonlinear relations of liquid water saturations with respect to current densities at both the anode and cathode are regressed. At low and high current densities, liquid water saturation at the anode linearly increases as a consequence of the linear increase of liquid water saturation at the cathode. In contrast, exponential relation is found to be more accurate at medium current densities