Location: Kashan, Isfahan
client: Moshfeq Industrial Development Co.
services: Site Supervision
DRI Plant (with Tunnel Kilns)
Here is a summary of the activities Vista Faraz Co. monitors and certifications it issues as field supervisor:
How to produce DRI using tunnel kilns
The operations department of the DRI plant consists of the following sections:
Incoming materials preparation area
Dehumidification of the concentrate
Crushing and granulation of pellets
Preparation of lime and coal
Loading, which consists of the following:
Lime and coal loading
Concentrate loading
Inspection
Lime and coal loading
Mold handling
Product preparation area
Ash discharge
Sponge iron discharge
Product crushing in a machine with three sections: feeder, jaw crusher, and hammer crusher.
Briquetting
There can be direct rotary or even multi-story kilns depending on the place of construction, with capacities of 5000 metric tons and more.
Refractory/fireproof containers for loading iron concentrate are made of silicon carbide or materials resistant to thermal shock.
Production process:
Raw materials that include powdered iron-ore concentrate (hematite or magnetite), oxide shell, soft pellet, coal and lime, are put into the dryer one by one to reach a humidity below 2%.
After that, the containers are placed on the car and taken into the kiln, so that the materials will be reduced by coal.
Reduction time: 40 to 50 hours
Maximum temperature of the kiln: 1220 degrees Celsius
Reduction temperature: 1140 to 1180 degrees Celsius
Kiln pressure: controlled
Material inlet temperature: ambient temperature
Material outlet temperature: about 70 degrees Celsius
DRI Kiln requirements:
After loading, the materials enter the kiln and are placed in the three zones of pre-heating, reduction and cooling, so that the reduction takes place.
Tunnel kilns:
By controlling the quality of raw materials, it is possible to increase the grade of sponge iron to over 95%. This type of DRI is fairly resistant to self-heating.
A briquetting machine can be added to the production line to change the product’s density. The gangue can be reduced by a magnetic separator. The product can be used in the induction furnace after briquetting.
Having a unit with a suitable capacity, the investment return time is less than three years. This method is cheaper than the Midrex method.