Highly metallised low Sulphur Directly Reduced Iron from Iron Ore Slime and Rejected or Middling Coal
1. |
Title of Product/Design/Equipment |
Highly metallised low Sulphur Directly Reduced Iron from Iron Ore Slime and Rejected/Middling Coal |
|
2. |
IPR Status Patent/Abroad IPR Details |
Patent Application No: 1320/KOL72013 & 1345/KOL/2013
|
|
3. |
Application/Uses |
Iron and steel making
|
|
4. |
Salient Technical Features including Competing Features |
The process utilises ~100% waste materials to yield a value added product. This invention is useful for converting steel plant wastes fines / mining waste fines such as iron ore slime/fines, middling and rejected coal containing more than 25 % ash into a highly metallised (Metallisation > 96%) low Sulphur (0.006%S) DRI suitable for induction furnace, electric arc furnace and blast furnace for iron and steel making. |
|
5. |
Level/Scale of Development |
Laboratory scale: 1 to 5 kg |
|
6. |
Environmental Considerations |
Generation of 150-200 kg of coal char per ton of DRI No liquid effluent generated. |
|
7. |
Status of Commercialization |
Ready for commercialization |
|
8. |
Major Raw Materials to be Utilized |
(i) Waste / lean iron ore fines such as iron ore slime (ii) Waste / lean grade coal containing 25 to 65% ash such as Middling Coal, Rejected Coal and likewise. |
|
9. |
Major Plant Equipment and Machinery Required |
(i) Muffle furnace or Tunnel Kiln, (ii) Ceramic crucibles, (iii) Pelletizer etc., |
|
10. |
Techno-Economics |
Cost of the DRI produced to be approximately Rs. 13,000 / ton. Chemical requirement cost is about Rs. against product cost of about Rs. per ton of iron oxide production.
|
|
11. |
Technology Package |
Complete flow-sheet with mass balance, Equipment details, Process description, Cost estimate and Product specification. Assistance in setting up the plant as per organization terms and conditions
|
Chemical requirement cost is about Rs. 30.9 against product cost of about Rs. 1.25.9 per ton of iron oxide production