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May 2007 - SIMA

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• Dust is generated during handling and<br />

transportation of iron ores, DRI, solid<br />

reducing agents and ash; the latter two<br />

only using alternate sources of reducing<br />

gases, other than natural gas. Typically,<br />

the material handling of an Energiron plant<br />

consists of the iron ore and product<br />

handling systems. These systems include<br />

bins, screening units, coating unit,<br />

conveyors, and transfer stations. Air<br />

pollution caused by dust is minimized by<br />

installing appropriate dust collectors in the<br />

main generation points, typically in trasfer<br />

locations and screening units.<br />

• Flue gases containing the polluting<br />

elements SO x and NO x , are derived from<br />

the combustion systems of the reducing<br />

gas generation units, gas heaters and<br />

rotary kilns. The amount of SO x and NO x<br />

can be decreased in gas based processes<br />

by an adequate control of combustion<br />

operations, and by desulfurization of the<br />

fuel gas stream to be used, both as<br />

process gas (reducing gas) and as fuel.<br />

The process chemistry of each technology<br />

will determine how difficult or how easy this<br />

control will be. In the case of the<br />

Energiron technology, SO x is selectively<br />

eliminated in the CO 2 absorption unit and<br />

NO x is easily controlled by low-NO x type<br />

burners, allowing compliance with even the<br />

strictest standards.<br />

• Suspended solids in the effluents from the<br />

water systems consist mainly of iron oxide<br />

and DRI particles, collected in the wet<br />

systems of the different sections of the<br />

plant. These solids can be dried and<br />

concentrated to be sold or reused as<br />

feedstock in the reduction units.<br />

Environmental Impact<br />

Emissions from Energiron plants are in<br />

accordance with the most stringent environmental<br />

regulations anywhere. This is achieved in large<br />

part due to the process design itself; while other<br />

processes require heat recovery equipment which<br />

tends to increase the NO x levels, the Energiron<br />

Process is efficient by design due to its process<br />

configuration and heat recovery systems.<br />

Depending on the type of plant, heat recovery<br />

systems consists of:<br />

• With external reformer - the efficiency is<br />

achieved by generation of steam, which is<br />

required for natural gas reforming and for<br />

CO 2 stripping. Prior to end-using, the steam<br />

is used in some steam turbines for power<br />

co-generation, reducing significantly<br />

electricity consumption.<br />

• With “in-situ” reforming, the steam required<br />

in CO 2 stripping is generated in the top gas<br />

heat recuperator.<br />

Thus, while achieving high overall thermal<br />

efficiency in the plant, there is no significant need<br />

for preheating the combustion air in the reformer<br />

or in the heater to high temperatures, thus<br />

eliminating the possibility of high NO x generation.<br />

For other DR processes, this is not the case and<br />

the choice between decreasing thermal efficiency<br />

or installing expensive de-NO x units remains.<br />

The tables summarize the environmental impact<br />

of Energiron plants, comprising solid wastes,<br />

emissions to the air and water, and noise. These<br />

levels comply with the strict standards imposed in<br />

such areas as the USA, Saudi Arabia, Malaysia<br />

and other nations with the most modern<br />

environmental standards, including new standards<br />

proposed but not yet enacted.<br />

Tenova HYL together with Danieli has been<br />

working on a project for a plant of 1.6 million tpy<br />

capacity being built for GHC in Abu Dhabi, where<br />

environmental controls are also among the<br />

strictest anywhere. Still, the values achieved are<br />

well within the requirements for compliance.<br />

Table I<br />

Solid Wastes (kg/ton DRI)<br />

Recycled Dumped Total<br />

• Dust collected 3.20 - 3.20<br />

• Iron oxide fines - 26.70 26.70<br />

• DRI cooling losses - 6.45 6.45<br />

• Others 0.25 0.35 0.60<br />

MAY-<strong>2007</strong>/34

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