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The following raw materials
used in Blast Furnace for the
production of pig iron: -
(i) Iron ore
(ii) Limestone
(iii) Dolomite
(iv) Quartzite
(v) Sinter
(vi) Coke
(vii) Pellets
(viii) Coal Dust / Coal Tar
Rawironisfoundinearth’scrust,asan
ore.
IronoremostlyfoundasFe2O3(the form
ofironoxidefoundasthe mineral
hematite).
Atpresent, blastfurnaceismostcommonlyused
furnacetoproduceiron.
TheBlast furnaceironmakingprocess basically
consists oftheconversion ofiron oxide to ironin
liquidform .
Thisrequires reductantforreduction of ironoxide
and heatforthe abovereductionreactionto take
place.
Theprimarysourcetofulfill boththese
requirements is carbon(inthe formofcoke).
Blastfurnaceisavertical counter-
currentheatexchangeraswellasa
chemicalreactorinwhich
burdenmaterialchargedfromthetopdescend
downwardandthegassesgeneratedatthe
tuyerelevelascendupward.
Blast
Furnace
Iron
Ore
• Ironorechunksdugsfromtheearthand
takentoprocessplant.
• Chunksarecrushedtosmallfractions,and
impuritiesareremovedbymagnetic
separatororothermeans.
• Thesmalliron fractionsareformedinto
marblesized pelletsinformingdrumsand
discs.Then thepelletsaretransportedto
stackyardof steelplant.
Ore crushed &
Transported from
mine to plant
Steel
Plant
Blast
Furnace
Iron
Ore
Mine
Stack
Yard
Material
Handling
System
Iron ore is collected from mines and crushed
Stack Yard
Processed iron ore are dumped at stack yard
Iron ore are transported through belt conveyor
Belt Conveyor
Material
Handling
System
Raw Materials are
Stored and
transported
inside steel plant
and fed into
Blast Furnace
through material
handling system
Blast
Furnace
Iron
Ore
Coal Coke
Oven
Plant
Coke
• Coalarecollectedfrommines.
• Then theyarewashed&crushedtopieces.
• Afterthatcoalistransportedtostackyard
ofsteelplant.
• Fromstack throughmaterialhandling
section, theyaretransportedtocokeoven
section,wherecoalisbakedand
convertedintocoke.
Processed &
Transported from
mine to plant
Steel
Plant
Blast
Furnace
Coal
Mine
Stack
Yard
Coke
Oven
Plant
Transportation by
Material Handling
System
Coke
Stack
Material
Handling
System
Coal is collected from mines
Coal is processed, washed and crushed and then
transported into stack yard of steel plant
Processed coal is dumped at stack yard and transported
to coke oven plant by material handling system
• Cokeissourceof thermalenergy insidetheBlast
Furnace,whichburnsandtheconvertedheatmelts the
ironore.
• Conventional cokemakingisdoneina cokeovenbattery.
Insideoven batterycoalissandwichedbetween heating
walls.
• Theyarecarbonized (atatemperaturearound1000o-
1100oC)uptoacertain degreeof de-volatizationto
produce metallurgicalcokeof desired mechanicaland
thermo-chemicalproperties.
• During CARBONIZATION, coals undergo
transformation into plastic state at around 350o-
400o C, swell and then re-solidify at around
500o-550oC to give semi- coke and then coke.
• In coke ovens,after coal is charged inside the
oven, plastic layers are formed adjacent to the
heating walls, and gradually the plastic layers
move towards the centre of oven from either
sideand ultimately meet each other at the centre.
• The quality and quantity of plastic layer is of
extreme importance and it determines the
inherentstrengthof coke matrix. For producing
coke of good quality, coals should have certain
degree of maturity, good properties and wide
range of fluidity.
Quenching of hot coke:-
Redhotcokeformedinsideoven
pushedoutbypushercar,and
collectedonquenchingcar.
The Quenching car travels and placed below the quench tower. The coke is
treated to high-pressure water jets to cool the coke while still in the quench car.
The coke is discharged from car and crushed into pieces and stacked.
Quench
Tower
Quenching Car
with coke
Blast
Furnace
Iron
Ore
Coke
Oven
Plant
Coke
Flux
Coal
• Fluxis addedintheblastfurnaceto remove
impurities,byproducingslag.
• Limeisthemostcommonlyusedflux
material.
• Limemaybe usedasaflux intheformof
CaO,limestone (CaCO3), dolomite
(magnesium calciumcarbonate)ordolomitic
lime (productobtainedfromburningor
roastingofdolomite).
 Limeisusedasafluxinsolid,
particulateformandreactswith
impuritiesinthechargetoformaslag.
 Itisimportantthattheslagbekept
fluid,notonlytoincreaseitsabilityto
scavengeimpuritiesfrommolten metal,
butalsotopermittheslagto bereadily
removedfromthefurnace.
n
t
Blast
Furnace
Material
Handling
System
Flux crushed &
Steel
Pla
Transported from
source to plant
Stack
Yard
FLUX
Sinterisanagglomerationofironore
fines,cokeandlimestoneintheformof
cakes.
Inordertoenhancetheproductivityof
blastfurnaces,ahighpercentageof sinter
chargeisaprerequisite.
Toensuresinterproductionburdenin
theblast furnacesat75percent,atotal
of 3milliontonnesofsinterwas
envisagedforof about2milliontonnes of
hotmetal.
Sinter Plant
Blast
Furnace
Iron
Ore
Coal
Coke
Oven
Plant
Coke
Flux
Sinter
Fines
from
different
sources
Sinter Plant
• Therawmaterialsusedareasfollows- Ironorefines
(-10mm),cokebreeze(-3 mm),Limestone&dolomite
fines(-3mm)andothermetallurgicalwastes.
• The proportionedrawmaterialsaremixedand
moistenedinamixingdrum.
• Themixis loadedonsintermachinethroughafeeder
ontoamovinggrate(pallet)andthenthe mixisrolled
through segregationplateso thatthecoarse
materialssettleatthe bottomandfinesontothetop.
• The top surfaceof themixisignited
through stationary burners at1200oC.
• As thepalletmovesforward, theairis
suckedthrough windboxsituatedunderthegrate.
• Ahightemperaturecombustionzoneis createdinthe
charge -bed dueto combustion of solid fuel of themix
and regeneration of heatof incandescentsinterand
outgoing gases.
• Dueto forward movementof pallet ,thesintering
process travelsvertically down.
• The differentzonescreatedon asinter-bed areshown
inthesimpleflow diagramof sinterplant.
 Thepelletsareusedasrawmaterialfor
Ironmaking intheplantsasanalternate
materialforSinterand/orLumpOre.
 Thepelletsarepreferredoversinterand
lumporeastheirshape,size,strengthand
excellentdesignedmetallurgical
propertiesinBlastfurnacesasburden.
 Itisalsoanironbearingmaterials.
 Themicro-fines whichcannotbeusedforsinter makingcan
beusedforpellet
manufacturingandthe
pellets formedwillbe
chargedintheBlast
FurnaceforIronMaking.
 Alltheraw materialischargedinto the
blastfurnace,from top,throughvariable
throatarmour or anyothermeans.
 Thepurposeofablastfurnaceisto
chemicallyreduceandphysically
convertironoxidesintoliquidiron
called"hotmetal".
 Theblast furnaceisahuge,steel stack lined
with refractory brick,whereironore, cokeand
limestone aredumpedintothe top, and
preheatedairisblownintothe bottom.
 Therawmaterials require6 to 8hoursto
descendto the bottom of the furnacewhere
they becomethe finalproductofliquidslag and
liquidiron.
 Theseliquidproductsare drainedfromthe
furnaceatregular intervals.
 Thehotairthatwasblownintothe
bottomofthefurnaceascendstothetop
in6to8secondsaftergoing through
numerouschemical reactions.
 Onceablastfurnaceis starteditwill
continuouslyrunfor fourtotenyears
withonlyshort stopstoperform
plannedmaintenance.
 Inrecentyears,manyalternativeiron makingprocesses havebeen
proposedanddevelopedtoreplacetheconventionaliron making
process–theblastfurnaceprocess.
 Blastfurnaceshaveplayedamajorpartinpigiron productionbecause
oftheirhighheatandgasutilizationefficiency, massproduction.
 Inpresent blastfurnaceprocesses havesomeunavoidableproblems,
environmentalpollutionbythecokeplants,lowerproduction
flexibilityandhighdegreeofrawmaterialspreparations.
o Theadvantages ofalternativeironmakingprocessis,it requiredtosatisfy the
criteriasuchastheuseofdifferentcoals,simplifiedmaterialpreparation,
metalwith littleimpurities, independentprocesssteps, closedenergysystem,
efficientpollution controlandnowastegeneration.
o Theyalsomay haveahigherproductivity perunitvolumethana blastfurnace
andthecapitalcostseemsto besignificantlylowerthantheconventional
process.
o Efficientwayto decreasethecostofrawmaterialsandto meetthe
environmentalrequirementsisto usealternativetechnologiesforironand
steelmaking.
o Forthealternativetechnologiesthecostsofrawmaterialsandpreparation is
notso highespeciallyiftheyareby-productsfromownorrelatedindustries.
Morethan90%ofworld'sironproductionis
throughBlastfurnacetechnologyroute.
DrivingforcesfordevelopmentofAlternative
Ironmakingtechnologies.
Costly and scarce coking coal
Possibility to use iron ore fines directly
Land-constraint
Environmental considerations
Water scarcity
Large scale of economy
Scientific/ engineering knowledge
 POSSIBLE SOLUTIONS :“Alternative for Iron Making”
1]PRODUCTIONOFNON-LIQUID IRON(DRI):-
 Direct ReducedIron (DRI)hasemergedasanexcellent substitutefor scrapfor
electricfurnaces.
 That’swhy,DRIproduction haszoomed throughout theworld (`~73 mtin2015),
 SL/RN, MIDREX,HYL, ITmk3 etc.
2]ALTERNATIVE METHODFORLIQUIDIRON(HOTMETAL):-
 Smelting Reduction(SR) processes: COREX, FINEX, Hismelt etc.
(usingnon-cokingcoal,obviatingtheneedforcokeovenbatteriesandsinterplants,needing
smallerland/area,Ironorefines canbeuseddirectly(exceptCOREX),Lesser pollution)
“DRI TECHNOLOGIES”
Both gas-based &coal-based DRI technology readily
available;
Scaleofoperation :-
Gas based : 0.8 – 2.0 mtpa/module
Coal based : 0.03 - 0.15 mtpa/module
Feed stock:-
Gas based processes – Pellet (8-15mm): 33 - 100 %;
Iron ore (6-30mm): 0 - 67% ; Natural gas / Coal gas
(not practiced yet)
Coal Based Processes (rotary kiln) - Iron Ore/Pellet (
6- 20 mm): 100%, • Non-coking Coal
GAS BASED DRI PROCESS
:-
RetortProcess
Fluidized BedProcess
ShaftReactor Process
“Available Smelting Reduction (SR)
Processes”
#4SRTechnologiescurrently commerciallyexploited or
ready forcommercialexploitation
COREX (Two stage): Operating commercially
FINEX (Two stage): Operating commercially
HISMELT (Single stage): Not Operating
commercially at present
ROMELT (Single stage): Not Operating
commercially present
•Single stage: Reduction & melting in the same vessel
•Two stage : Reduction in one vessel; melting in the 2nd vessel
Iron Making PPT- (Girish,Shreya,Joydeep).pptx
Iron Making PPT- (Girish,Shreya,Joydeep).pptx

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Iron Making PPT- (Girish,Shreya,Joydeep).pptx