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Stainless steel displays
unique engineering properties in terms of strength, toughness and overall
corrosion resistance over a wide range of temperatures along with good
forming and welding characteristics. Against growing competition from
alternative materials like aluminums and plastics, stainless steel remains
the only choice where corrosion resistance properties are required.
Among all steel categories,
stainless is the most growth intensive. Although tonnage wise, stainless
steels are a very small member of the steel family, accounting for barely
2 to 3 per cent of total steel output worldwide. The total quantity of
world crude stainless steel output jumped from about 1.0 million tonne
(mt) in 1950 to 21.6 mt in the year 2000, registering and impressive annual
growth rate of over 6 per cent
The stainless steel
sector in India has experienced a quantum jump in the last two decades.
Production during 1978 was only 15,000 tonnes, which reached level of
around 1.2 mt during 2002-2003 representing a share of 5.6 per cent out
of the total world stainless steel production of 21.5 mt [2]. There is
a tremendous potential to increase the consumption of stainless steel
in the sectors such as construction, transport, processing industries
etc. The Present per capita consumption in India is lowest in the world,
around 0.66 Kg as compared to 10 to 18 Kg in developed countries [4].
The expanding processing
sectors like chemical, petro-chemical, oil and gas, food processing, transport,
etc. require a large amount of stainless steel. The extent of stainless
steel demand in India is projected 1.69 mt for 2006 - 2007.
Stainless steel making
technologies have been exploited to enhance overall efficiency, tonnage
capability, flexibility of input materials, reduction in processing cost,
and improvement in product quality.
New technologies are
available and also under development for meeting over increasing demands
of stainless steel making, so as to achieve the following goals:
-
Saving on the
material cost,
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Reducing the energy
consumption,
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Increasing the
productivity,
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Improving the
product quality,
-
Reducing environmental
emissions,
-
Introducing automation,
computer aided quality control and production planning,
-
Reducing the investment
cost.
Two types of processes,
developed for stainless steel making are as follows:
In duplex process,
after melting in primary unit, refining is carried out in different vessel.
Duplex process have certain disadvantages with respect to the ratio of
ferro-alloys to scrap in the case of VOD and higher argon, ferro-silicon
consumption and shorter convertor life in case of AOD, lengthy process
time in secondary vessel convertor. However, in order to overcome these
demerits and produce different grades with grater economy and better quality,
triplex process is used.
In triplex process,
after melting in primary unit, refining are carried out in two different
vessels. In the first vessel, decarburisation and major refining take
place and final stages of desulphurisation and degassing take place in
second vessel.
Compare to duplex,
triplex process has following merits:
-
Increase productivity
-
Increase number
of heats per day
-
Increase scrap
to liquid metal yield
-
Improved quality
of metal
-
High operational
flexibility
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Comparatively
lower cost of production.
Thermodynamics
and reaction kinetics of stainless steel making process
Conditions in the
production of stainless steels are largely governed by thermodynamics
equilibrium of oxygen reactions with carbon and chromium at different
temperatures and partial pressure of CO. With rising temperatures and
decreasing CO partial pressures, equilibrium conditions can therefore
shifted to lower carbon levels at the same amount of chromium.
The decarburisation
of stainless steel involves the techniques to minimize chromium oxidation.
There are three basic techniques: increasing the temperature, decreasing
of CO-partial pressure by dilution with inert gas and using the vacuum.
In the past the temperature technique was used for production of stainless
steel in arc furnace, but it was abandoned due to uneconomical nature
of production .
The dilution technique
is used by AOD / MRK process and all converter processes. The injection
of inert gas (argon or nitrogen) lowers the partial pressure of CO in
the bath, thus allowing higher chromium contents to be in equilibrium
with low contents of carbon.
Applying vacuum to
metal bath also remove CO, allowing high chromium contents to be in equilibrium
with low carbon contents. It is especially effective when carbon content
is low.
Classification
of stainless steels
Stainless steels can
be divided into five families. Four are based on the characteristic crystallographic
structure/microstructure of the alloys in the family: ferritic, martensitic,
austenitic or duplex (austenitic plus ferritic). The fifth family, the
precipitation - hardenable alloys, is based on the type of heat treatment
used, rather than microstructure.
IF - AOD I MRK
- LRF Route
Induction Furnace
(IF):
Technology of melting
of metals and alloys by electric induction system is fairly old in the
world. In India also many steel plants and ordnance factories to manufacture
high alloy and tool steel installed high frequency induction melting furnaces.
The requirement of stainless steel in country was fairly high. But stainless
steel production was not good. Induction melting furnaces started making
stainless steels since early eighties by using imported stainless steel
scrap.
At present stainless
steel is produced by melting stainless steel scrap, mild steel scrap and
ferro alloys in induction furnace; and transferring the liquid metal to
AOD / MRK vessel for refining and purging by inert gas to the liquid metal.
After AOD / MRK treatment, further refining is done in LRF and then produce
billet by con cast process. In India stainless steel produced, in induction
furnace route, is 277,000 tonnes in 2002-2003.
Now a day's contribution
by the secondary producer for production of crude steel is drastically
increased (37.6 per cent in 2002-2003). Out of those induction furnace
units contributes (15.6 per cent).
The cost of melting
the charge in induction furnace is lower than that in arc furnace due
to the following reasons:
-
Reasonable power
consumption due to faster melting, lower tapping temperature and higher
power density. Fe-Cr melting is difficult in an arc furnace due to
the absence of stirring. Also, lime and fluxes added to protect the
lining take away substantial amount of heat.
-
Lower tapping
temperature of 15300C. In arc n furnace, chromium comes in contact
with atmospheric oxygen and gets oxidized. To recover this Cr, at
the end of melting, metal is super heated above 15300C and reductant
like carbon or Fe-Si is added.
-
No use of graphite
electrodes in induction furnace.
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No flux / lime
requirement for melting in induction furnace.
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Lower refractory
cost as acidic ramming mass is much cheaper when compared to basic
ramming mass and bricks.
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4 per cent higher
Cr recovery compared to that of arc furnace as negligible amount of
Cr is oxidized in induction furnace.
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Reduced pollution
due to fumes, dust, slag. Gases formed and sucked in the arc furnace
cause greater pollution.
Argon Oxygen Decarburisation
(AOD) / Metal Refining Konvertor (MRK):
After melting the
scrap in induction furnace the liquid metal of temperature 1600-1650oC
is tapped and then subsequently charged in to the AOD / MRK. To carry
out decarburisation and other reactions either oxygen or mixture of oxygen-nitrogen
/ argon is blown through the bottom tuyer of the converter. Excellent
gas mixing promotes fast decarburisation, deoxidation and desulphurisation
and improves recoveries of alloying elements. The steel refined by AOD
/ MRK process is low in oxygen, nitrogen and argon. AOD / MRK process
ensures low content of suspended oxides, high level of purity in stainless
and other steels.
Ladle Refining
Furnace (LRF):
Processed metal, as
above, is then transferred to ladle refining furnace for desulphurisation
of melt. Gentle stirring with nitrogen / argon in the LRF removes inclusions
and thus improves the quality. LRF can be operated with single graphite
electrode working on dc power supply. Single electrode reduces the refractory
erosion and carbon pick up.
Treatment of AOD /
MRK heats in LRF reduces cost and improves quality of the melt. Table
6 shows the progress of chemistry changes during 200 series stainless
steel production in LF-MRK-LRF route [11].
Remarks
With the high projected
demand of stainless steel, numbers of expansion plans from the existing
producers have come to force. At present, in spite of some of the demerits,
duplex processes are used for production of stainless steel. However,
triplex processes can be considered to be the most advanced process route
for high quality stainless steelmaking.
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