| Customization: | Available |
|---|---|
| Model: | 2.5*60-6.0*95 |
| Object: | Sponge Iron |
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1.What's the DRI?
Direct reduced iron (DRI) is a type of alternative iron made by heating iron ore, mill scale pellet or concentrated iron powder so that the oxygen and carbon burns off while the temperature is kept below iron's melting point. Direct-reduced iron is also known as sponge iron and is sold as briquettes, lumps, or pellets. It is typically used in smaller scale steel mills to enhance the condition of the steel that is manufactured.
During the reduction process in the production of direct reduced iron, either coal or a special gas - commonly containing a combination of carbon monoxide and hydrogen - is used. This mixture functions as a reducing agent and facilitates the decrease in the iron's oxygen and carbon content. The result is a type of iron that is 90-97% pure, containing only minuscule amounts of carbon and other impurities.
In the modern era, direct reduced iron is considered an alternative method of making iron. The process of crafting iron via the direct-reduction route has a distinct advantage over the more traditional, blast furnace mode of production. Not only is the resulting iron more plentiful in total iron content, but it entails a much cheaper production process than the operation of a large blast furnace.
2.The raw material
The raw material to produce DRI is Iron ore, mill scale, or concentrated iron powder which in Fine pellet or Lumps shape.
3.The chemical reactions of DRI production
The chemical reactions involved in the direct reduction of iron are the following:
With H2 (Gas Based)
3Fe2O3 + H2 → 2Fe3O4 + H2O
Fe3O4 + H2 → 3 FeO + H2O
FeO + H2 → Fe + H2O
With CO (Coal Based)
3Fe2O3 + CO →2Fe3O4 + CO
Fe3O4 + CO → 3 FeO + CO2
FeO + CO → Fe + CO2
With Solid Carbon in reaction
CO2 + C → 2CO
4.Direct reduction processes
There are several processes for direct reduction of iron ore:
-- gas-based rotary kiln furnace processes
-- coal based rotary kiln furnaces
Generic illustrations of the types of process are shown in the graphics below.
(1) For your required concentrated iron powder process flow:
Generally speaking, the Fe content of your sample > 65%, firstly, the concentrated iron powder will be made to small pellet by pelletizer (iron powder will be mixed with Coal powder by certain ratio, please note, the coal powder function as reduction agent), and then after making pellet, and after screen, it will be conveyed into the Chain grate, which function is preheating the pellet and making the pellet more strength.
Then after preheating, the pellet will be calcined in the rotary kiln during temperature 950ºC-1100ºC, and the reduction chemical reaction will be occurred, as the above introduction, during this process, the inside of pellet will shape many small hole, which called DRI.
1. One ton raw material (Mill scale or Concentrated iron powder) should be mixed with reduction agent coal 500-600kg;
2. Heating source consumption: Coal: 220kg/t, or Gas: 140m3/t
3. Reduction coal technical require: Volatile (Vad) >30%, Ash(Ad) < 20%, C >50%, S<1%, Moisture <10%-15%, TS+6mr >70%;
4. Lime consumption: about 120kg for desulfidation and dephophorization
5. Electricity: whole plant total power * 0.75/ day (500tpd plant total power 1312KW), s to produce one ton DRI need about 47.23KWH electricity.
6. Final Product: TFe≥92%, MFe≥89%, M≥94% ,S≤0.02% ,P≤0.05%, C≥0.04%
Hongke DRI Plant Flow:
Concentrated Iron Powder or Mill Scale Coal based DRI production
| Specification | Capacity(t/d) | Incline of body(°) | Speed(r/min) | Main motor(kw) | Remarks |
| Φ2.5*60 | 168 | 3.5 | 0.516-1.549 | 75 | Alumyte-alumina forge kiln |
| Φ3*48 | 700 | 3.5 | 0.726-3.63 | 110 | Kiln with 5-stage cyclone precalciner |
| Φ3*60 | 3.5 | 0.492-1.476 | 75 | Alumyte-alumina forge kiln | |
| Φ3*100.94 | 450 | 4 | 0.3-1.503 | 90 | Multiple-drum cooling |
| Φ3.2*46 | 1000 | 3.5 | 0.36-3.57 | 160 | kiln with preheater precalcine |
| Φ3.2*52 | 1200 | 3.5 | 0.343-0.34 | 125 | kiln with preheater |
| Φ3.3*50 | 1300 | 3.5 | 0.676-3.38 | 160 | kiln with plateau suspension preheater |
| Φ3.3*52 | 1300 | 3.5 | 0.266-2.66 | 125 | kiln with preheater precalcine |
| Φ3.5*54 | 1500 | 3.5 | 0.55-3.4 | 220 | kiln with preheater precalcine |
| Φ3.6*70 | 1800 | 3.5 | 0.25-1.25 | 125 | Generating kiln for using ofterheat |
| Φ4*60 | 2500 | 3.5 | 0.396-3.96 | 315 | kiln with preheater precalcine |
| Φ4.15*58 | 5 | 0.35-0.7 | 110 | Zinc leaching(calcine rotary kiln) | |
| Φ4.2*60 | 3000 | 4 | 0.4-3.98 | 375 | |
| Φ4.3*60 | 3500 | 3.5 | 0.396-3.96 | 375 | kiln with preheater precalcine |
| Φ4.5*66 | 4000 | 3.5 | 0.41-4.1 | 560 | kiln with preheater precalcine |
| Φ4.8*74 | 5000 | 4 | 0.396-3.96 | 630 | kiln with preheater precalcine |
| Φ5.0*74 | 6000 | 4 | 0.35-4 | 710 | kiln with preheater precalcine |
| Φ5.6*87 | 8000 | 4 | Max4.23 | 800 | kiln with preheater precalcine |
| Φ6.0*95 | 10000 | 4 | Max5 | 950*2 | kiln with preheater precalcine |
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