Freeze-Lining Formation in Submerged Arc Furnaces Producing Ferrochrome Alloy in South Africa

Author(s):  
Joalet Dalene Steenkamp ◽  
Quinn Gareth Reynolds ◽  
Markus Wouter Erwee ◽  
Stefan Swanepoel
JOM ◽  
1962 ◽  
Vol 14 (2) ◽  
pp. 126-128 ◽  
Author(s):  
J. Glasser ◽  
W. E. Few
Keyword(s):  

2021 ◽  
Author(s):  
Gerrit R Surup ◽  
Nicholas Smith-Hanssen ◽  
Merete Tangstad
Keyword(s):  

2021 ◽  
Author(s):  
Mads Fromreide ◽  
Svenn Anton Halvorsen ◽  
Manuel Sparta ◽  
Vetle K Risinggård ◽  
Pilar Salgado ◽  
...  
Keyword(s):  

JOM ◽  
1996 ◽  
Vol 48 (12) ◽  
pp. 49-51
Author(s):  
Markus A. Reuter ◽  
Carla Pretorius ◽  
Chloë West ◽  
Peter Dixon ◽  
Morné Oosthuizen

JOM ◽  
2017 ◽  
Vol 69 (9) ◽  
pp. 1712-1716 ◽  
Author(s):  
Joalet Dalene Steenkamp ◽  
Christopher James Hockaday ◽  
Johan Petrus Gous ◽  
Thabo Witness Nzima

Minerals ◽  
2021 ◽  
Vol 11 (11) ◽  
pp. 1286
Author(s):  
Marcus Sommerfeld ◽  
Bernd Friedrich

The production of ferroalloys and alloys like ferronickel, ferrochromium, ferromanganese, silicomanganese, ferrosilicon and silicon is commonly carried out in submerged arc furnaces. Submerged arc furnaces are also used to upgrade ilmenite by producing pig iron and a titania-rich slag. Metal containing resources are smelted in this furnace type using fossil carbon as a reducing agent, which is responsible for a large amount of direct CO2 emissions in those processes. Instead, renewable bio-based carbon could be a viable direct replacement of fossil carbon currently investigated by research institutions and companies to lower the CO2 footprint of produced alloys. A second option could be the usage of hydrogen. However, hydrogen has the disadvantages that current production facilities relying on solid reducing agents need to be adjusted. Furthermore, hydrogen reduction of ignoble metals like chromium, manganese and silicon is only possible at very low H2O/H2 partial pressure ratios. The present article is a comprehensive review of the research carried out regarding the utilization of bio-based carbon for the processing of the mentioned products. Starting with the potential impact of the ferroalloy industry on greenhouse gas emissions, followed by a general description of bio-based reducing agents and unit operations covered by this review, each following chapter presents current research carried out to produce each metal. Most studies focused on pre-reduction or solid-state reduction except the silicon industry, which instead had a strong focus on smelting up to an industrial-scale and the design of bio-based carbon for submerged arc furnace processes. Those results might be transferable to other submerged arc furnace processes as well and could help to accelerate research to produce other metals. Deviations between the amount of research and scale of tests for the same unit operation but different metal resources were identified and closer cooperation could be helpful to transfer knowledge from one area to another. Life cycle assessment to produce ferronickel and silicon already revealed the potential of bio-based reducing agents in terms of greenhouse gas emissions, but was not carried out for other metals until now.


2021 ◽  
Author(s):  
Svenn Anton Halvorsen ◽  
Manuel Sparta ◽  
Vetle K Risinggård ◽  
Mads Fromreide
Keyword(s):  

2017 ◽  
Vol 4 (9) ◽  
pp. 170313 ◽  
Author(s):  
K. Karalis ◽  
N. Karkalos ◽  
G. S. E. Antipas ◽  
A. Xenidis

A transient mathematical model was developed for the description of fluid flow, heat transfer and electromagnetic phenomena involved in the production of ferronickel in electric arc furnaces. The key operating variables considered were the thermal and electrical conductivity of the slag and the shape, immersion depth and applied electric potential of the electrodes. It was established that the principal stimuli of the velocities in the slag bath were the electric potential and immersion depth of the electrodes and the thermal and electrical conductivities of the slag. Additionally, it was determined that, under the set of operating conditions examined, the maximum slag temperature ranged between 1756 and 1825 K, which is in accordance with industrial measurements. Moreover, it was affirmed that contributions to slag stirring due to Lorentz forces and momentum forces due to the release of carbon monoxide bubbles from the electrode surface were negligible.


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