Jungang Wang

Prof. Jungang Wang


Research Focus & Metrics

Academic Career Length

10Years (2017-Present)

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

Representative Publications

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14 September 2018 in ACS Catalysis
Verified
Journal Article
Closed access
CQChuan Qin
Chuan Qin
BHBo Hou
Bo Hou
JWJungang Wang
Jungang Wang
QWQiang Wang
Qiang Wang
Gang WangGang Wang
Gang Wang
DLDebao Li
Debao Li

1 February 2019 in Applied Catalysis A: General
Verified
Journal Article
Closed access
LWLiqin Wang
Liqin Wang
HGHeqin Guo
Heqin Guo
QXQilong Xie
Qilong Xie
JWJungang Wang
Jungang Wang
BHBo Hou
Bo Hou
DLDebao Li
Debao Li

20 January 2024 in ACS Catalysis
Verified
Journal Article
Closed access
YFYang Feng
Yang Feng
YZYang Zhang
Yang Zhang
JWJungang Wang
Jungang Wang
LLLixia Ling
Lixia Ling
RZRiguang Zhang
Riguang Zhang
BWBaojun Wang
Baojun Wang

9 September 2019 in ACS Applied Materials & Interfaces
Verified
Journal Article
Closed access
CQChuan Qin
Chuan Qin
BHBo Hou
Bo Hou
JWJungang Wang
Jungang Wang
Gang WangGang Wang
Gang Wang
ZMZhongyi Ma
Zhongyi Ma
DLDebao Li
Debao Li

20 July 2017 in Catalysis Science & Technology
Verified
Journal Article
Closed access
PDF file
HLHansheng Li
Hansheng Li
BHBo Hou
Bo Hou
JWJungang Wang
Jungang Wang
XHXin Huang
Xin Huang
CCCongbiao Chen
Congbiao Chen
DLDebao Li
Debao Li
A series of meso–macroporous silica supports with the same macroporous diameter but different mesoporous diameters were prepared by introducing phase separation into a sol–gel process and used to prepare cobalt catalysts for Fischer–Tropsch synthesis. The mesoporous diameter could be controlled in the range 6.5–35.0 nm while the macroporous diameter was kept at approximately 500 nm. The mesoporous porosity of the meso–macroporous silica supports greatly influenced the size, reducibility and dispersion of cobalt nanoparticles, and therefore resulted in different catalytic performances for Fischer–Tropsch synthesis. The meso–macroporous catalyst with an appropriate mesoporous size of 8.5 nm displayed a higher catalytic activity due to the best combination of the Co dispersion and reduction degree. The product distribution strongly depended on the mesoporous diameter due to the following two reasons: 1) the difference in the H2/CO ratio on the active sites due to the diffusional limitations of CO in the mesopores; 2) the Co crystallite size effect. In addition, large pellet catalysts (800–1700 μm) exhibited similar product distributions to small pellet catalysts (180–250 μm), which indicated that the macropores played an important role in reducing internal diffusion limitations for large pellet catalysts.

1 July 2018 in International Journal of Hydrogen Energy
Verified
Journal Article
Closed access
JWJin Wang
Jin Wang
JWJungang Wang
Jungang Wang
XHXin Huang
Xin Huang
CCCongbiao Chen
Congbiao Chen
ZMZhongyi Ma
Zhongyi Ma
DLDebao Li
Debao Li