大东 KOd

Mx. 大东 KOd


Research Focus & Metrics

Academic Career Length

5Years (2022-Present)

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

Representative Publications

View All Publications
5 November 2024 in Journal of Iron and Steel Research International
Verified
Journal Article
Closed access
PDF file
HWHai-Feng Wang
Hai-Feng Wang
JQJian Qiu
Jian Qiu
大K大东 KOd
大东 KOd
FWFeng Wang
Feng Wang
LLLi-Jin Lu
Li-Jin Lu
XLXiu-Ping Li
Xiu-Ping Li

15 July 2022 in Metals
Verified
Journal Article
Open access
PDF file
FWFeng Wang
Feng Wang
XSxue-feng shi
xue-feng shi
大K大东 KOd
大东 KOd
JGJianjun Gao
Jianjun Gao
JZJun Zhang
Jun Zhang
ZHZhang Huining
Zhang Huining
Carbon monoxide is the major hazardous component in flue gas exhausting from the iron ore sintering. This study aims to reduce the CO emission by changing the sinter parameters by sintering pot tests; specifically, the sinter quality, CO concentration, and total emission in sintering flue gas were analyzed in detail. The sinter strength properties, including the shatter index and the tumble index, are analyzed by the sintering pot test and the sintering flue gas discussion. The results show that the CO emission can be suppressed by modifying the sinter parameters, such as carbon content, coke breeze and coal breeze ratio, water addition, and sintering negative pressure. The good sinter parameters with the lower CO emission are 2.8% carbon content and 7.5% water in the sintering mixture. A higher coke breeze to coal breeze ratio, or only coke breeze fuel in the sinter mixture, is beneficial for the lower CO emission with a negative fan pressure of −12 kPa.

31 March 2023 in Ironmaking & Steelmaking: Processes, Products and Applications
Verified
Journal Article
Closed access
大K大东 KOd
大东 KOd
FWFeng Wang
Feng Wang
JPJianlei Pan
Jianlei Pan
HWHaiFeng Wang
HaiFeng Wang
ZAZhiwei An
Zhiwei An
In order to analyse the feasibility of sintering for municipal sludge treatment, a sintering pot was used for the experiment. The results showed that the main effects of sludge addition on the sintering process and sinter quality come from the changes in the heat addition and moisture content of the granulated sinter. The addition of sludge could improve the granulation efficiency of the sinter mixture and the particle size composition of the sinter. When the proportion of sludge was 7%, the addition of sludge completely replaced the water required for mixing, and the overall sintering index was the best. In this case, after reducing fuel consumption by 10%, except for the content of P, the sinter quality and the sintering index could met the requirements of steel production. Finally, the use of fuel and raw materials with high P content needed to be reduced with the addition of sludge.

5 November 2024 in Metals
Verified
Journal Article
Open access
PDF file
LLLijin Lu
Lijin Lu
FWFeng Wang
Feng Wang
FWFeng Hai Wang
Feng Hai Wang
JQJian Qiu
Jian Qiu
大K大东 KOd
大东 KOd
Hydrogen-based smelting reduction has received widespread attention as an important technology for realizing low-carbon development in hydrogen metallurgy. In this study, the thermodynamics of smelting reduction was firstly analyzed by using FactSage 8.1 thermodynamic software, on the basis of which smelting reduction experiments of iron oxides by using bottom-blown hydrogen were carried out. The experiments used oxidized pellets as experimental materials, and the effects of the reduction process were analyzed in terms of the reduction temperature, the reduction time, and the hydrogen flow rate. The experimental results show that under the experimental conditions of a temperature of 1550 °C and a hydrogen flow rate of 0.2 Nm3/h, the reduction rate of iron oxides in the process of reducing iron oxides by hydrogen is significantly faster in the first 10 min than after 10 min. The hydrogen utilization rate reached a maximum of 41.87%, then decreased continuously and finally maintained at about 20%. Using the method of model fitting, it was found that the hydrogen-based molten reduction conformed to the phase boundary reaction model (Gα=1−(1−α)1/2), the corresponding mechanism function is fα=2(1−α)1/2, where α stands for the reduction conversion, and the reaction rate constant k(T) is 2.37 × 10−4 s−1 under the experimental conditions.