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== References ==
== References ==
1- Valipour MS, and Saboohi, Y, "Numerical investigation of nonisothermal reduction of hematite using Syngas: the shaft scale study", Modelling Simul. Mater. Sci. Eng. 15(5) p.487, 2007.
(http://iopscience.iop.org/0965-0393/15/5/008)


2- Valipour, MS, "Mathematical Modeling of a Non-Catalytic Gas-Solid Reaction: Hematite Pellet Reduction with Syngas", Scientia Iranica, 16(2c), 108-124, 2009. (http://www.scientiairanica.com/Issues/00113/2009/v16/n2.aspx)
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Revision as of 21:11, 23 January 2012

Direct-reduced iron (DRI), also called sponge iron,[1] is produced from direct reduction of iron ore (in the form of lumps, pellets or fines) by a reducing gas produced from natural gas or coal. The reducing gas is a mixture majority of hydrogen (H2) and carbon monoxide (CO) which acts as reducing agent. This process of directly reducing the iron ore in solid form by reducing gases is called direct reduction.

The conventional route for making steel consists of sintering or pelletization plants, coke ovens, blast furnaces, and basic oxygen furnaces. Such plants require high capital expenses and raw materials of stringent specifications. Coking coal is needed to make a coke strong enough to support the burden in the blast furnace. Integrated steel plants of less than one million tons annual capacity are generally not economically viable. The coke ovens and sintering plants in an integrated steel plant are polluting and expensive units.

Process

Direct reduction, an alternative route of iron making, has been developed to overcome some of these difficulties of conventional blast furnaces. DRI is successfully manufactured in various parts of the world through either natural gas or coal-based technology. Iron ore is reduced in solid state at 800 to 1,050 °C (1,470 to 1,920 °F) either by reducing gas (H2+CO) or coal. The specific investment and operating costs of direct reduction plants are low compared to integrated steel plants and are more suitable for many developing countries where supplies of coking coal are limited.

The direct reduction process is intrinsically more energy efficient than the blast furnace[citation needed] because it operates at a lower temperature, and there are several other factors which make it economical:

  • Direct-reduced iron has about the same iron content as pig iron, typically 90–94% total iron [2] (depending on the quality of the raw ore) as opposed to about 93% for molten pig iron, so it is an excellent feedstock for the electric furnaces used by mini mills, allowing them to use lower grades of scrap for the rest of the charge or to produce higher grades of steel.
  • Hot-briquetted iron (HBI) is a compacted form of DRI designed for ease of shipping, handling, and storage.[2]
  • Hot Direct Reduced Iron (HDRI) is iron not cooled before discharge from the reduction furnace, immediately transported to a waiting electric arc furnace and charged thereby saving energy.
  • The direct reduction process uses pelletized iron ore or natural "lump" ore. One exception is the fluidized bed process which uses (requires) sized iron ore particles. Select few ores are suitable for direct reduction.
  • The direct reduction process can use natural gas contaminated with inert gases, avoiding the need to remove these gases for other use. However, any inert gas contamination of the reducing gas lowers the effect (quality) of that gas stream and the thermal efficiency of the process.
  • Supplies of powdered ore and raw natural gas are both available in areas such as Northern Australia, avoiding transport costs for the gas. In most cases the DRI plant is located near natural gas source as it is more cost effective to ship the ore rather than the gas.

India is the world’s largest producer of direct-reduced iron, a vital constituent of the steel industry.[3] Many other countries use variants of the process, so providing iron for local engineering industries.

Problems

Directly reduced iron is highly susceptible to oxidation and rusting if left unprotected, and is normally quickly processed further to steel.[citation needed] The bulk iron can also catch fire since it is pyrophoric.[4]

History

Producing sponge iron and then working it was the earliest method used to obtain iron in the Middle East, Egypt, and Europe, where it remained in use until at least the 16th century. There is some evidence that the bloomery method was also used in China, but China had developed blast furnaces to obtain pig iron by 500 BCE.

The advantage of the bloomery technique is that iron can be obtained at a lower furnace temperature, only about 1,100°C or so. The disadvantage, relatively to using a blast furnace, is that only small quantities can be made at a time.

Uses

Sponge iron is not useful by itself, but can be processed to create wrought iron. The sponge is removed from the furnace, called a bloomery, and repeatedly beaten with heavy hammers and folded over to remove the slag, oxidise any carbon or carbide and weld the iron together. This treatment usually creates wrought iron with about three percent slag and a fraction of a percent of other impurities. Further treatment may add controlled amounts of carbon, allowing various kinds of heat treatment (e.g. "steeling").

Today, sponge iron is created by reducing iron ore without melting it. This makes for an energy-efficient feedstock for specialty steel manufacturers which used to rely upon scrap metal.

See also

References

1- Valipour MS, and Saboohi, Y, "Numerical investigation of nonisothermal reduction of hematite using Syngas: the shaft scale study", Modelling Simul. Mater. Sci. Eng. 15(5) p.487, 2007. (http://iopscience.iop.org/0965-0393/15/5/008)

2- Valipour, MS, "Mathematical Modeling of a Non-Catalytic Gas-Solid Reaction: Hematite Pellet Reduction with Syngas", Scientia Iranica, 16(2c), 108-124, 2009. (http://www.scientiairanica.com/Issues/00113/2009/v16/n2.aspx)

  1. ^ "What is direct reduced iron (DRI)? definition and meaning". Businessdictionary.com. Retrieved 2011-07-11.
  2. ^ a b What Is HBIA?
  3. ^ http://www.midrex.com/uploads/documents/MIDREXStatsBook2009rev4.pdf
  4. ^ Hattwig, Martin; Steen, Henrikus (2004), Handbook of explosion prevention and protection, Wiley-VCH, pp. 269–270, ISBN 9783527307180.

External links