Sponge iron, is the product of reducing iron oxide in the form of iron ore and steel plant wastes into metallic iron, below the melting point of iron and typically in the range of 800–1200 °C.
Iron Ore Pellet is used for reduction. After reduction of iron ore pellet the product resembles sponge because of pores left behind after removal of oxygen. As such it is called Sponge Iron.
Sponge iron making is a process in which iron ore lumps (typically 5mm-18mm size) are tumbled with a 'select' grade of iron-coking coal little dolomite inside an inclined rotary kiln and control combusted in the presence of air for about 12 hours before the products are air cooled, magnetically separated and screened.
Sponge iron is formed through the reduction of iron ore to metallic iron through reaction with carbon in the form of coal, etc. at approx. 1100 degree Celsius. Over the years, the shortage of expensive melting scrap has made sponge iron a significant raw material for manufacturing high quality steel.
Sponge iron is used in the iron and steel industry as a substitute for scrap in induction and electrical arc furnaces. Over the years, the shortage of expensive melting scrap has made sponge iron a significant raw material for manufacturing high quality steel.
Capacity: 2,31,000 Metric Tonnes Per Annum (Two Lakh Thirty One Thousand Metric Tonnes Per Annum).
- This process utilizes non-coking coal as reducing agent along with lumpy rich grade iron ore.
- The reduction is carried out in an inclined horizontal rotary kiln, which rotates at a predetermined speed. A temperature profile ranging from 800-1050 degree centigrade is maintained along the length of the kiln at different zones and as the material flows down due to gravity the ore is reduced.
- The hot reduced sponge iron along with semi-burnt coal, discharged from kiln is cooled in water-cooled cylindrical rotary cooler to a temperature of 100–200 degree centigrade.
- The discharge from cooler consisting of sponge iron, char other contaminations are passed on through magnetic separators so that sponge iron can be separated from other impurities.
The basic reactions in this process is as follows:
C + O2 = CO2
CO2 + C = 2CO
Fe2 O3 + CO = Fe3O4 + CO2
Fe2 O4 + CO = FeO + CO2
FeO + CO = Fe + CO2
Raw Material Requirements
As in case of any process, here also quality of raw materials plays a vital role in obtaining the rated capacity and product quality. The iron ore shall have resistance for physical & thermal de-crepitation and good reducibility and the coal should be of reactive nature along with the characteristics of high fusion temperature and less amount of ash.
|Total iron||65 - 67 %|
|Sio2 + al2 o3||2 - 3 %|
|Cao + mgo||0.5 - 1 %|
|Sulphur||0.02 % max.|
|Phosphorous||0.04 % max.|
|Size||5 - 20 mm|
|Shatter Index||+ 95 %|
|Tumbler Index||+ 88 %|
|Abrasion Index||+ 5 % max|
|Reducibility Index||+ 94 %|
|Thermal Degradation Index||5 %|
|Fixed Carbon||+ 40%|
|Ash Softening Point||1250 deg cent|
|Calorific Value||5200 k . Cals / mole|
|Reactivity||2.2 co / gm . Deg c|
|Cao||40 - 45 %|
|L.O.I.||40 - 45 %|
|Insolubles||5 - 7 %|
|Size||0.5 - 4 mm|
|Total Iron||90 - 93 %|
|Metallic Iron||80 - 84 %|
|Metallisation||90 - 92 %|
|Gangue||3 - 4 %|
|Sulphur||0.02 - 0.03 %|
|Phosphorous||0.035 - 0.05 %|
|S/No||SPECIFICATION||SI DRCLO||SI BACHELI (NORMAL)||SI PELLETS|