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New ferrochrome smelter for Assmang
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The Assmang ferrochrome facility about 8 km south
west of Machadodorp, Mpumalanga, RSA.
The 60 m-high building
housing the new smelter
may be seen on the
right-hand of the picture.

The Assmang sinter plant.

The roof of the furnace with the Bateman Titaco electrode system and the
feed chutes.
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A consortium of Bateman Titaco and Outokumpu Engineering Contractors
Oy has supplied a new smelter at Assmang Chrome Division's Machadodorp
Works, Mpumulanga, RSA. The plant uses the latest technology in agglomeration,
sintering and preheating of the feed ore supplied to the furnace, resulting
in improved chromium recovery and a lower consumption of kilowatt hours
per tonne of metal produced. Furnace stability and ease of operation
during smelting are also enhanced.
This R300M turnkey contract for Assmang Chrome, an Avmin / Assore joint
venture, effectively doubles the ferrochrome output at the Machadodorp
plant to about 300 000 t/yr . The smelter includes a 54 MVA furnace,
a preheater and a 350 000 t/yr pelletising plant.
The submerged-arc closed furnace is a Bateman Titaco design and features
Bateman Titaco electrode holders using Söderberg paste. A significant
advantage of this design is that the smelting process does not generate
significant amounts of toxic chromium six. With a pretreated charge
the furnace can be sealed gas tight. It also reduces environmental pollution
as the process gas is cleaned, rendering it suitable for use as a heating
fuel.
A feature of the furnace is its freeze lining, which is expected to
extend the campaign life of the furnace lining considerably. A Bateman
Titaco mudgun and taphole drill unit was also supplied. The mudgun is
electrically operated and eliminates any potential fire hazards in front
of the taphole. The drill is pneumatically operated.
The preheater and pelletising plant embody Outokumpu technology and
supply the furnace with sintered pellets, significantly increasing chrome
recovery and reducing electrical energy consumption.
The fine-ore feed to the plant is milled and filtered to remove excess
water, mixed with a binder and passed into a pelletising drum to produce
green pellets of between 10 and 15 mm. Under- and oversized pellets
are reprocessed.
The green pellets are fed to an energy-efficient steel-belt sintering
furnace and are dried, preheated, sintered and cooled to produce sintered
pellets with a hard and porous structure and excellent high-temperature
strength. The pretreated pellets now contain iron in a readily reducible
form and the high specific surface of the finely ground chromite increases
the reduction rate in the smelting furnace and avoids non-uniform reduction.
The cooled pellets are stored on stockpiles, part of which is used to
form a protective under-layer in the sinter machine and the balance
sent to the furnace for smelting.
The hot gases from the cooling compartments are recycled to the drying,
preheating and sintering compartments and greatly improve the energy
efficiency of the sintering system. The decomposition of the volatile
hydroxides and carbonates during sintering also reduces the demand for
electrical energy during subsequent smelting in the furnace.
Stockpiled sintered pellets, with other raw materials, are conveyed
and fed into a preheater above the furnace. Here the pellets are heated
to a temperature of 600 °C by combusting the scrubbed gases captured
in the furnace. Preheating the pellets reduces the electrical energy
consumption of ferrochrome production by about 20 % compared to conventional
plants. It also increases the capacity of the furnace, results in a
smoother arc-furnace operation and reduces electrode consumption and
maintenance downtime.
A building 60 m high had to be constructed to house both the furnace
and the preheater. Being essentially a brown-fields project, care had
to be taken not to disrupt ongoing production at the works. The contract
for the project was awarded in June 2000 and completed in October 2001
with the opening ceremony for the new smelter held on 29 January 2002.
The furnace took 14 months to complete and the pelletising plant a further
two months.
A very similar project was completed in 1999 by Bateman Titaco and Outokumpu
Engineering Contractors Oy for Hernic Ferrochrome and has been followed
by another, but of double the size, for SA Chrome, due for completion
later this year.

For further details kindly contact George Farmer, General Manager,
Bateman Ferrous, on +27-11-899-2531 or email ferroalloys@batemanengineering.com
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