Shiwei Li

Prof. Dr. Shiwei Li

School of Metallurgy and Energy Engineering, Kunming University of Science and Technology, Kunming, China

Research Focus & Metrics

Academic Career Length

13Years (2014-Present)

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

Representative Publications

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1 February 2020 in Journal of Hazardous Materials
Verified
Journal Article
Closed access
HLHaoyu Li
Haoyu Li
HLHailin Long
Hailin Long
LZLibo Zhang
Libo Zhang
SYShaohua Yin
Shaohua Yin
SLShiwei Li
Shiwei Li
HXHuimin Xie
Huimin Xie

4 May 2023 in Materials Horizons
Verified
Journal Article
Closed access
PDF file
JRJianfeng Ran
Jianfeng Ran
XWXuxu Wang
Xuxu Wang
YLYuanhong Liu
Yuanhong Liu
SYShaohua Yin
Shaohua Yin
SLShiwei Li
Shiwei Li
LZLibo Zhang
Libo Zhang
Layout structure of this review. Highlighting the fabrication, design principles and applications of microreactors for the synthesis of inorganic, organic and composite micro/nanomaterials.

6 May 2024 in Environmental Chemistry Letters
Verified
Journal Article
Closed access
PDF file
JRJianfeng Ran
Jianfeng Ran
YLYun Li
Yun Li
XWXuxu Wang
Xuxu Wang
HDHaisheng Duan
Haisheng Duan
YCYing Chen
Ying Chen
JZJiaping Zhao
Jiaping Zhao

1 January 2018 in Ultrasonics Sonochemistry
Verified
Journal Article
Open access
HLHaoyu Li
Haoyu Li
SLShiwei Li
Shiwei Li
JPJinhui Peng
Jinhui Peng
Srinivasakannan ChandrasekarSrinivasakannan Chandrasekar
Srinivasakannan Chandrasekar
LZLibo Zhang
Libo Zhang
SYShaohua Yin
Shaohua Yin
A new method of preparation high purity nickel sulfate assisted by ultrasonic was studied. The process mechanism was analyzed by Inductively Coupled Plasma (ICP), X-ray diffraction (XRD), Scanning electron microscopy (SEM), and Energy dispersive X-ray spectrometry (EDS).The reaction mechanisms of oxidizing leaching and ultrasonic leaching were explored, respectively. Results showed that ultrasonic treatment peel off the oxide film on the surface of nickel. The leachate under strongly agitated, the yield rate of nickel sulfate was accelerate. And the reaction area was increased by the cavitation effect, the liquid-solid reaction was promoted, and the activation energy was reduced. The leaching rate of nickel reached 46.29% by conventional leaching, which takes about 5h. Under the same conditions, the ultrasonic leaching rate reached 40%, only half of the conventional leaching time. Concentration of leaching agent, reaction temperature, ultrasonic power, leaching time had significant effect on the enhancement of the leaching reaction with ultrasonic radiation. The leaching rate of 60.41% under the optimum experiment conditions as follows: sulfuric acid concentration 30%, hydrogen peroxide 10%, leaching temperature 333K, ultrasonic power 200W and leaching time 4h. The kinetic study of the system was investigated, and the reaction rates of conventional leaching and ultrasonic leaching were controlled by diffusion, and the apparent activation energies were 16.2kJ/mol and 11.83kJ/mol.

1 February 2021 in Journal of Hazardous Materials
Verified
Journal Article
Closed access
HLHailin Long
Hailin Long
HLHaoyu Li
Haoyu Li
PMPengcheng Ma
Pengcheng Ma
ZZZhufen Zhou
Zhufen Zhou
HXHuimin Xie
Huimin Xie
SLShiwei Li
Shiwei Li

1 January 2016 in Green Processing and Synthesis
Verified
Journal Article
Open access
PDF file
AMAiyuan Ma
Aiyuan Ma
LZLibo Zhang
Libo Zhang
JPJinhui Peng
Jinhui Peng
XZXuemei Zheng
Xuemei Zheng
SLShiwei Li
Shiwei Li
WCWeiheng Chen
Weiheng Chen
In this research, the extraction of zinc from the blast furnace dust in the ammonia leaching system containing different leaching agents (NH 3 , (NH 4 ) 3 AC, (NH 4 ) 2 CO 3 , (NH 4 ) 2 SO 4 , NH 4 Cl) was investigated. Meanwhile, the effects of different total ammonia concentrations, ammonia/ammonium ratios, solid-liquid ratios, stirring speeds, and leaching temperatures on the extraction of zinc were studied. The results showed that ammonium sulfate was particularly effective and the extraction efficiency of zinc is up to 86.48% under the following conditions: total ammonia concentration of 5.0 mol/l, ammonia/ammonium ratio of 1:1, solid-liquid ratio of 1:5, temperature of 45°C, leaching time of 60 min, and stirring speed of 350 rpm.