2. Metallurgy & Material Engineering
▪ Group Members
– Usama Hassan(332)
– Asfand Shahid(333)
– JunaidIllahi (334)
– Asad Jamil (335)
– Ahmer Ejaz(336)
3. COREX PROCESS
▪ Smelting Reduction Process
▪ Combination of Melter Gasifier & Reduction
Shaft
▪ Lump iron ore or pellets, non-coking coal,
and oxygen as main inputs
▪ Counter Current Principle
▪ Alternative to Blast Furnace
4. Why do we seek alternative to Blast Furnace?
▪ CHALLENGES
– The conventional blast furnace route is too costly and
energy-intensive to keep pace with dynamic market changes,
where even short- and medium-term fluctuations show their
dramatic impact on iron production.
– The need to use coke and sinter makes it much more
difficult to fulfil ever stricter environmental regulations and
to achieve economical competitiveness .
– Rising energy demand, continuous price increases for
natural gas and raw materials, and steadily decreasing
quality of iron ore.
5. Why do we seek alternative to Blast Furnace?
▪ SOLUTION
– Corex is besides FINEX the only reliable alternative to the
conventional blast furnace route.
– Corex will make you less dependent on price trends for raw
materials.
– Corex provides you with the key technology for producing
hot metal in an economically and ecologically sustainable
manner.
– It frees from the need to invest in the operation and
maintenance of coking and sinter plants because these
additional facilities are not needed at all.
8. Differences between COREX& Blast Furnace
The maindifferences betweenCorexand a conventional blast
furnace routeare
▪ Non-coking coal can be used directlyas a reducing agent
and energy source
▪ Up to 80% of the ironoxide fraction can be lumpore; no
sintering is required
▪ Pure oxygeninsteadof nitrogen-richhot blast
9. Salient Features
▪ Developed by Siemens VAI.
▪ Commercially most successful among SR technologies.
▪ Work is carriedout in 2 reactors.
▪ Reductionshaft & Melter-gasifier.
▪ Commercial units in operation
– Korea: POSCO
– India: JSWSteel & Essar Steel ltd
– SouthAfrica: Mittal-SALDANHA
– China: Baosteel
15. WORKING •Charge is chargedintoa
reductionshaftwhere theyare
reducedto directreducediron
(DRI)by a reductiongasmovingin
counterflow.
•DischargescrewsconveytheDRI
fromthereductionshaftintothe
Melter–Gasifier.
•In Melter - Gasifierfinalreduction
and meltingtakesplace.
•Hotmetaland slagtappingare
done as in conventionalblast
furnacepractice.
•The gasleavingthereduction
shaftis cooledand cleanedand is
usedfor a widerangeof
applications.
•Itsexhaustgasesareusedin
MIDREXProcess.
16. WORKING ELABORATED
▪ ReductionShaft
– Ironore, pelletsand additives(limestoneand dolomite) are continuously
charged fromthe top.
– Some amount of cokeis also addedto the shaft to avoid clustering.
– Thereductiongas is injected throughthe bustle locatedabout 5 meters
above thebottomof theshaftat 850°Cand over3-barpressure.
– Thegas movesin the countercurrent direction to the topof the shaft and
exitsfromthe shaft at around250°C.
– Theironbearingmaterial gets reducedto over 95%metallizationinthe
shaft and is termedas DRI.
– Subsequently, six screws dischargethe DRI fromthe reductionshaft into
the Melter - Gasifier.
17. WORKING ELABORATED
▪ The Melter- Gasifier can largelybe dividedintothree reaction zones
– Gaseousfreeboardzone(upperpartor dome)
– Charbed(middlepartaboveoxygentuyeres)
– Hearthzone(lowerpartbelowoxygentuyeres)
▪ The hot DRI at around 600-800 °C alongwithlimestoneand
dolomiteare continuouslyfed intothe Melter-GasifierthroughDRI
down pipes.
▪ The DRI down pipes are uniformlydistributed along the
circumference near the top of the melter-gasifier so as to ensure
uniformdistribution of material over thechar bed.
18. WORKING ELABORATED
▪ Additionallynon-coking coal, quartziteand required quantityof coke
are continuouslychargedby meansof lock hoppersystem.
▪ The operatingpressure,in the melter-gasifier is in excess of 3 bars.
▪ Oxygen plays a vital role in COREXprocessfor generation of heat
and reduction gases. It is injectedthroughthe tuyeres, whichgasifies
the coal char generatesCO.
▪ The hot gases ascend upward throughthe char bed. The sensible heat
of the gases is transferred to the char bed, whichis utilized for
meltingiron and slagand other metallurgical reactions. The hot
metal and slag are collected in the hearth.
22. DISADVANTAGES
▪ It has the limitationindistributingthecoaland DRI in theoptimised
manner inthe Melter-Gasifier.
▪ Thecoalconsumption in Corexis muchhigherthanin any other iron
makingprocess.
▪ Thesystemis maintenanceoriented,includingcoolinggas compressor for
recyclingpart of COREXgas for cooling the hot gasesfromthe melter-
gasifier.
▪ It is providedwithvery sophisticated gas cleaning facilities. Thereare three
gas cleaningstreamsfor cleaning the total gas generated inthe process.
▪ Theprocessis sensitiveto the qualityof inputs particularlywith respect to
quality
23. THERE IS ALWAYS A GOOD REASON FOR COREX
▪ Corex fulfils all additional requirements beyond an economical and
reliable iron makingunit. Examples include JSWin India, where two
Corex plantswere erectedfor a steelworks in an isolated areawithno
access to naturalgas or electricity; Baosteel in China, where a new
steelworkswaserected in a waterprotectionareawitha demand for
electricity; and ArcelorMittal SouthAfrica, where a Corex-DR
combination formsthe iron making basis for a steelworks in an
environmentallyrestricted area. The expansionto a Corex-DR
combination plant at JSWunderlines the flexibilityof Corexto
respond to actual market demands in the ironand steel business.