Kinetics Calculation of the Non-isothermal Reduction of Pellet

2016 ◽  
Vol 35 (5) ◽  
pp. 507-514 ◽  
Author(s):  
Liu Yingli ◽  
Wang Jingsong ◽  
Guo Wentao ◽  
Dong Zeshang ◽  
Xue Qingguo

AbstractThe reduction tests of pellet were carried out from room temperature to 1,373 K in the condition of traditional blast furnace (TBF) and oxygen blast furnace (OBF) by thermogravimeter measurement. The apparent activation energy E, pre-exponential factor A and the controlling steps of reaction were determined by the non-isothermal method of Coats–Redfern. In the condition of TBF, the reduction is controlled by solid diffusion to interfacial chemical reaction at initial stage, and gas diffusion at final stage. In the condition of OBF, the controlling step switched from solid diffusion to gas diffusion + interfacial chemical reaction in the beginning and the interfacial chemical reaction at the late stage. Meanwhile, the transition temperature points of the controlling step were predicted. The transition temperatures are 750℃ and 900℃ in TBF and 630℃ (earlier 120℃ than in TBF) and 900℃ (after the insulation) in OBF.

2020 ◽  
Vol 39 (1) ◽  
pp. 447-456
Author(s):  
Zhenlong An ◽  
Jingbin Wang ◽  
Yanjun Liu ◽  
Yingli Liu ◽  
Xuefeng She ◽  
...  

AbstractThe top gas recycling-oxygen blast furnace (TGR-OBF) is a reasonable method used to reduce both coke rate and energy consumption in the steel industry. An important feature of this process is shaft gas injection. This article presents an experimental study on the gas–solid flow characteristics in a TGR-OBF using a two-dimensional cold model. The experimental conditions and parameters were determined using a series of similarity criteria. The results showed that the whole flow area in the TGR-OBF can be divided into four distinct flow zones, namely, the stagnant zone, the plug flow zone in the upper part of the shaft, the converging flow zone and the quasi-stagnant flow zone, which is similar to that in a traditional blast furnace. Then the effects of batch weight and the ratio (X) of the shaft injected gas flow rate to the total gas flow rate on solid flow behaviour were investigated in detail. With the increase in batch weight, the shape of the stagnant zone tends to be shorter and thicker. Furthermore, with the increase in X value from 0 to 1, the stagnant zone gradually becomes thinner and higher. The results obtained from the experiments provide fundamental data and a validation for the discrete element method–computational fluid dynamics-coupled mathematical model for TGR-OBFs for future studies.


JOM ◽  
2017 ◽  
Vol 70 (1) ◽  
pp. 29-33 ◽  
Author(s):  
Guang Wang ◽  
Yingli Liu ◽  
Zhenfeng Zhou ◽  
Jingsong Wang ◽  
Qingguo Xue

2016 ◽  
Vol 43 (6) ◽  
pp. 458-464 ◽  
Author(s):  
Long Chen ◽  
Qingguo Xue ◽  
Wentao Guo ◽  
Xuefeng She ◽  
Jingsong Wang

2012 ◽  
Vol 39 (5) ◽  
pp. 313-317 ◽  
Author(s):  
Y H Han ◽  
J S Wang ◽  
R Z Lan ◽  
L T Wang ◽  
X J Zuo ◽  
...  

2020 ◽  
Vol 92 (1) ◽  
pp. 2000326
Author(s):  
Wei Zhang ◽  
Jing Dai ◽  
Chengzhi Li ◽  
Xiaobing Yu ◽  
Zhengliang Xue ◽  
...  

2017 ◽  
Vol 46 (8) ◽  
pp. 761-770 ◽  
Author(s):  
C. L. Li ◽  
Q. G. Xue ◽  
Y. L. Liu ◽  
Z. S. Dong ◽  
G. Wang ◽  
...  

2017 ◽  
Vol 24 (6) ◽  
pp. 608-616 ◽  
Author(s):  
Xue-feng She ◽  
Xiu-wei An ◽  
Jing-song Wang ◽  
Qing-guo Xue ◽  
Ling-tan Kong

Sign in / Sign up

Export Citation Format

Share Document