Non-isothermal reduction process analysis of iron-bearing burden with charging iron coke hot briquette under simulated blast furnace conditions

Author(s):  
Hong-tao Wang ◽  
Man-sheng Chu ◽  
Ji-wei Bao ◽  
Zheng-gen Liu ◽  
Hong-ming Long
2007 ◽  
Vol 14 (2) ◽  
pp. 13-19 ◽  
Author(s):  
Man-sheng Chu ◽  
Xian-zhen Guo ◽  
Feng-man Shen ◽  
Jun-ichiro Yagi ◽  
Hiroshi Nogami

2010 ◽  
Vol 50 (5) ◽  
pp. 686-694 ◽  
Author(s):  
Shengli Wu ◽  
Hongliang Han ◽  
Haifa Xu ◽  
Hongwei Wang ◽  
Xiaoqin Liu

2020 ◽  
Vol 2,2020 (2,2020 (125)) ◽  
pp. 5-9
Author(s):  
Vaniukov A ◽  
Kovalyov D ◽  
Vaniukova N ◽  
Khodyko I ◽  
Bezshkurenko O

The objective of the present work is to research a quantitate ratio of degree direct reduction inside of SRP and degree of indirect reduction outside of SRP on the top of the blast furnace.The reactions of direct and indirect reduction occurring during the heat treatment of self reducing pellets (SRP) have been studied. In this investigation Blast furnace (BF) sludge which contains particles of coke, has been included in the SRP blend as a source of solid reductant and iron bearing oxides. In the SRP as a part ot the blast furnace burden occur the reactions simultaneously: inside of SRP-direct reduction by Csolid; gasification of carbon and indirect reduction by CO; and outside of SRP-indirect reduction of iron bearing oxides by reducing gas coming from the hearth of blast furnace through the column of charged materials. The experimental setup is shown in Fig. 1. It con-sists of a electrical heating furnace, which can be moved up and down. The quartz tube passes through the furnace. The reaction zone is in the middle of the furnace. Neutral argon atmosphere is created and for indirect reduction argon changed - on hydrogen. Gases of argon, hydrogen are introduced into the furnace separately. Wire of nickel alloy chromosome joins the scales test. A thermocouple is located in the tube.The crucible of wire chrome-nickel was permeable.Metohd. The experiments was performed continuously from the start temperature (~200 ˚C) to the experimental temperature (500 ˚C; 700 ˚C; 900 ˚C; 1100 ˚C) in argon free environment. Upon reaching the desired temperature argon was replaced by hydrogen during 30 minutes. After that the reduced probe of SRP was cooled in argon. Results. The integrated degree of reduction is equal 100%, which includes 98,6 % direct reduction by solid carbon under temperatures 1100°C. The chemical analysis of the reduced SRP showed the degree of integrated reduction change from 85,79 % (900 °C) to 92,50 % (1000 °C) and 84,6% (1100°C) and metallization 83,30 % (900 °C), 89,90 % (1000 °C), 80,75 % (1100 °C).These data correspond to results of degree of reduction SRP depends on temperature


2015 ◽  
Vol 55 (6) ◽  
pp. 1157-1164 ◽  
Author(s):  
Sung Hoon Chung ◽  
Ki Hyun Kim ◽  
Il Sohn

2015 ◽  
Vol 47 (1) ◽  
pp. 467-484 ◽  
Author(s):  
Zongliang Zhang ◽  
Jiale Meng ◽  
Lei Guo ◽  
Zhancheng Guo

2020 ◽  
Vol 15 (2) ◽  
pp. 501-513 ◽  
Author(s):  
Achmad Shofi ◽  
Yayat Iman Supriyatna ◽  
Agus Budi Prasetyo

The aim of the reduction process is to concentrate nickel at high temperatures with a certain carbonaceous material as a reducing agent. The use of chemicals like Na2SO4 and NaCl in the reduction process can increase the content and recovery of nickel in ferronickel concentrates. A selective reduction of laterite nickel was carried out in a non-isothermal and an isothermal using palm kernel shell charcoal as a reductant and with Na2SO4 and NaCl as additives. Firstly, the raw material is made into a pellet and dried in an oven at 100 °C for two hours. The pellets are weighed before and after the reduction process. The non-isothermal reduction process used the Thermal Gravimetric Analysis (TGA) method from a temperature of 100 to 1300 °C, with a heat rate of 10 °C per minute. The isothermal reduction at temperatures 500, 600, 700, 950, 1050, and 1150 °C occurred with a reduction time of 30, 60, and 90 minutes. The analysis is Inductively Coupled Plasma (ICP) to determine the content of nickel and iron from the reduction process, X-ray Diffraction (XRD) to see changes in the phases formed after the selective reduction process, and Scanning Electron Microscopy (SEM-EDX) for viewing the microstructure of the phase. The Differential Thermal Analyzer-Temperature Gravimetric Analysis (DTA-TGA) results show the endothermic at 256 °C, and the exothermic peak at 935 °C with a total mass loss of 42.15% at 1238 °C. The shrinking core model was used for the kinetic studies of the reduction process. The closest kinetic model to the experimental results is the Ginstling-Brounshtein model, with an activation energy value of 8.73 kcal/mol. Copyright © 2020 BCREC Group. All rights reserved 


1993 ◽  
Vol 79 (10) ◽  
pp. 1151-1156 ◽  
Author(s):  
Kentarou NOZAWA ◽  
Koichiro SHIBATA ◽  
Masakata SHIMIZU ◽  
Heinrich Wilhelm GUDENAU

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