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ELECTRIC			
STEELMAKING	
The	Processing	Route	
	
BEGINNER	LEVEL	
Author:	Eng.	Matteo	Sporchia	
	
	
	
Copyright	–	P4S	–	PRODUCTS	4	STEELMAKING	
All	Rights	Reserved
2	
SUMMARY	
	
INTRODUCTION	…………………………………………………………………………………..	PAG.	3	
	
RAW	MATERIALS	………………………………………………………………………..……….	PAG.	5	
	
PRIMARY	METALLURGY	……………………………………………………………………..	PAG.	10	
	
SECONDARY	METALLURGY	………………………………………………………………..	PAG.	22	
	
CONTINUOUS	CASTING	……………………………………………………………………..	PAG.	24
3	
INTRODUCTION	
	
Nowadays,	about	23%	of	the	total	worldwide	crude	steel	production	is	made	by	the	
Electric	Steelmaking	processing	route	which	mainly	involves	the	following	stages:	
	
• RAW	MATERIALS	
• PRIMARY	METALLURGY	
• SECONDARY	METALLURGY	
• CONTINUOUS	CASTING
4
5	
RAW	MATERIALS	
	
Raw	material	may	be	up	to	100%	scrap	or	various	mixes	of	hot	metal,	pig	iron,	DRI	
(hot	and/or	cold)	and	HBI.	
Worldwide,	scrap	covers	around	75%	of	the	raw	materials	for	EAF,	while	DRI	and	HBI	
covers	around	15%	and	the	balance	(10%)	is	covered	by	pig	iron	and	hot	metal.	
	
SCRAP	
Scrap	is	the	mostly	used	raw	materials	for	the	EAF	charge.	It	classification	depends	
on	 the	 grades	 of	 steel	 manufactured	 and	 the	 sorts	 of	 charge	 scrap	 available	
commercially	in	the	market.	The	following	properties	should	be	entailed	for	the	sake
6	
of	the	scrap	material	classifications:	
• Content	of	alloying	elements	possible	to	be	reclaimed	in	the	steel	smelting	
process;	
• Content	of	harmful	elements	(including	sulphur,	phosphorus,	copper,	zinc);	
• Geometry	of	scrap	(relevant	density	and	size).	The	knowledge	of	the	scrap	
material	geometry	enables	optimum	filling	of	the	EAF	charge	baskets.
7	
DIRECT	REDUCED	IRON	(DRI)	
	
	
	
Direct	Reduced	Iron	(DRI)	is	the	product	
of	the	direct	reduction	of	iron	ore	in	the	
solid	 state	 by	 carbon	 monoxide	 and	
hydrogen	 derived	 from	 natural	 gas	 or	
coal.		
Most	 gas-based	 direct	 reduction	 plants	
are	 part	 of	 integrated	 steel	 mini-mills,	
located	 adjacent	 to	 the	 electric	 arc	
furnace	(EAF)	steel	plant.
8	
DRI	can	be	either	hot	or	cold	charged	to	the	EAF.	Some	steel	companies	ship	DRI	from	
their	captive	direct	reduction	plants	to	their	remote	steel	mills	and	a	small	volume	of	
DRI	is	sold	to	third	parties.	There	are	many	small	rotary	kiln	furnaces	producing	DRI,	
known	 as	 sponge	 iron,	 using	 coal	 as	 energy	 and	 reductant	 source.	 Some	 of	 the	
sponge	iron	plants	are	captive	to	steel	mills.	
HOT	BRIQUETTED	IRON	(HBI)	
Hot	Briquetted	Iron	(HBI)	is	a	premium	form	of	DRI	that	has	been	compacted	at	a	
temperature	greater	than	650°	C	at	time	of	compaction	and	has	a	density	greater	
than	5,000	kilograms	per	cubic	metre	(5,000	kg/m3).
9	
	
	
	
	
HBI	is	compact	and	the	briquettes	are	
easy	 to	 feed	 into	 the	 furnace.	 In	
contrast,	 scrap	 is	 most	 unwieldy	 and	
sometimes	 needs	 cutting	 down,	 an	
expensive	process.	
It	 also	 frequently	 breaks	 the	
electrodes.	 By	 using	 HBI	 both	 the	
availability	of	the	smelting	furnace	and	
the	safety	of	employees	while	charging	
can	be	increased.
10	
PRIMARY	METALLURGY	
Electric	 Arc	 Furnace	 (EAF)	 is	 a	 central	 part	 of	 the	 production	 route	 of	 the	 Electric	
Steelmaking	process	that	is	an	alternative	to	the	dominant	Basic	Oxygen	Steelmaking	
(BOS)	route.	
EAF	 is	 generally	 used	 to	 produce	 carbon	 steels	 and	 alloy	 steels	 primarily	 by	
recycling	ferrous	scrap.	In	the	EAF,	scrap	and	sometimes	other	raw	materials	such	as	
DRI,	HBI	and	pig	iron	are	melted	and	converted	into	high	quality	steel	by	using	high-
power	electric	arcs	formed	between	a	cathode	and	one	(for	 direct	 current	 DC)	or	
three	(for	alternating	current	AC)	graphite	electrodes	(anodes).
11	
The	EAF	processing	route	could	be	summarized	as	follows:	
	
• CHARGING	OF	RAW	MATERIALS	
• MELTING	
• REFINING	
• DESLAGGING	
• TAPPING
12
13	
CHARGING	OF	RAW	MATERIALS	
The	charging	mix	(scrap	plus	other	raw	materials	
as	indicated	above)	is	put	into	the	furnace	from	
the	 top	 using	 a	 steel	 basket.	 Burnt	 lime	 and	
fluorspar	 are	 also	 added	 to	 help	 the	 slag	
formation.	 Usually	 more	 than	 one	 basket	 are	
used	to	charge	the	furnace	completely.	Once	the	
charge	of	the	first	basket	has	completely	melted	
down	and	a	flat	bath	is	reached,	another	bucket	
of	 scrap	 can	 be	 charged	 into	 the	 furnace	 and	
melted	down.	Some	furnaces	are	equipped	with	
continuous	charging.
14	
MELTING	
Melting	 is	 carried	 out	 by	 supplying	
energy	 to	 the	 furnace	 interior.	 This	
energy	 can	 be	 electrical	 or	 chemical.	
Electrical	 energy	 is	 supplied	 through	
the	 graphite	 electrodes	 and	 normally	
has	 a	 very	 large	 contribution	 in	 the	
melting	 phase.	 Chemical	 energy	 is	
supplied	 through	 many	 sources	 which	
include	 oxy-fuel	 burners	 and	 oxygen	
lances.
15	
The	entire	duration	of	the	process	can	be	divided	into	three	main	stages:	
	
Heating	stage:	The	scrap	is	heated	by	the	arc	and	oxy-fuel	burners	at	the	top	of	the	
furnace.	 The	 heating	 is	 done	 by	 radiation,	 convection	 (due	 to	 the	 hot	 gas	 going	
through	the	scrap	porosities)	and	conduction	(due	to	contact	points	between	scraps).	
The	temperature	at	the	top	increases	to	reach	the	melting	temperature	of	the	scrap.	
In	this	stage	the	gas	–	solid	phases	exist.	
Melting	 stage:	The	 melting	 starts	 at	 the	 top	 surface	 of	 the	 scrap	 pile,	 and	 molten	
liquid	penetrate	towards	the	bottom	of	the	furnace	and	its	height	increases	whereas	
the	height	of	the	scrap	pile	decreases.	In	this	stage,	there	are	gas	–	solid	and	solid	–
liquid	phases	in	the	bath.
16	
Finishing	stage:	The	scrap	is	completely	covered	by	the	melt	and	only	the	solid	–liquid	
phase	 exists	 until	 all	 the	 scrap	 is	 completely	 melted.	 At	 this	 point,	 usually	 bath	
temperature	and	bath	sample	is	taken.	The	analysis	of	the	bath	chemistry	allows	the	
furnace	operator	to	determine	the	amount	of	O2	needed	to	be	blown	during	refining.	
	
Lower	voltages	(short	arc)	are	selected	
for	the	first	stage	of	melting	to	protect	
the	 roof	 and	 the	 walls	 from	 the	 arcs.	
Subsequently	 voltage	 can	 be	 increased	
(long	 arc)	 and	 the	 electrodes	 raised	
slightly	increasing	the	length	of	the	arc	
and	increasing	power	to	the	melt.
17	
REFINING	
	
Refining	 operation	 is	 carried	 out	 following	 the	 melting	 phase	 after	 the	 flat	 bath	
conditions	are	achieved.	At	this	stage,	excessive	carbon	and	other	elements	(such	as	
phosphorous,	silicon,	manganese)	oxidize.	The	oxidation	of	the	carbon	is	also	known	
as	decarburization.
18	
At	the	start	of	the	melting	process,	the	arcs	are	covered	by	the	scrap,	so	the	radiation	
from	the	arcs	to	the	lateral	walls	is	low,	but	when	the	scrap	starts	melting,	the	heat	
efficiency	decreases	since	the	radiation	to	the	walls	increases.	Thus,	a	foaming	slag	is	
used	to	cover	the	arcs	as	more	heat	can	be	transferred	to	the	bath	and	scrap.	
Foaming	slag	is	formed	by	injection	of	carbon	and	oxygen,	First,	the	carbon	inside	
the	bath	is	oxidized	by	oxygen	blowing.	Oxygen	also	oxidized	certain	amount	of	iron	
and	 FeO	 is	 formed.	 The	 carbon	 injected	 reduces	 iron	 oxide.	 These	 two	 reactions	
generate	bubbles	of	CO	which	go	upward	and	foam	the	slag.	
The	function	of	the	slag	(mainly	composed	by	lime	CaO)	is	to	refine	the	steel	from	the	
sulphur	(desulfurization)	and	absorbs	the	oxides,	formed	as	a	result	of	deoxidation	
(also	known	as	killing	process).
19	
The	typical	composition	of	EAF	slag	is	CaO	(45	%	to	58	%)	SiO2	(5	%	to	15	%)	FeO	(10	%	to	28	%)	
MgO	(5%	to	8%)	and	MnO	(2	%	to	5	%),	Besides	it	also	contains	CaF2,	S,	and	P.
20	
DESLAGGING	
The	furnace	is	tilted	backwards	and	slag	is	poured	out	of	the	furnace	through	the	slag	
door.	Removal	of	the	slag	eliminates	the	possibility	of	P	reversion.	
	
TAPPING	
Once	 the	 desired	 steel	 composition	 and	 temperature	 have	 been	 achieved	 in	 the	
furnace,	the	tap	hole	or	the	EBT	(eccentric	bottom	tapping)	is	opened,	the	furnace	is	
tilted,	and	the	steel	is	poured	into	a	teeming	ladle	for	transfer	to	the	secondary	steel	
making	unit.	During	the	tapping	process,	ferro	alloy	additions	are	made	based	on	
the	bath	analysis	and	the	desired	steel	grade.	Deoxidizing	agent	are	added	to	the	
steel	to	lower	the	O2	content	prior	to	further	processing.	Common	deoxidizers	are	Al,
21	
ferrosilicon	and	silico	manganese.	While	making	C	steel	heats	a	minimum	of	slag	carry	
over	is	aimed.	A	new	slag	cover	is	built	during	tapping.	For	ladle	furnace	operations,	a	
calcium	aluminate	slag	is	a	good	choice	for	the	control	of	S.	Slag	forming	compounds	
are	added	in	the	ladle	at	tapping	so	that	a	slag	cover	is	formed	prior	to	transfer	to	the	
ladle	furnace.
22	
SECONDARY	METALLURGY	
The	ladle	is	transferred	to	a	device	called	Ladle	Furnace	(LF),	where	it's	places	under	a	cover	
equipped	with	three	graphite	electrodes	columns	which	are	connected	to	an	AC	transformer.	
The	 primary	 functions	 of	 the	 LF	 is	 the	 reheating	 of	 liquid	 steel	 through	 electric	 power	
conducted	 by	 the	 graphite	 electrodes	 and	 homogenization	 of	 steel	 temperature	 and	
chemistry	through	inert	gas	stirring.	In	fact	the	ladle	bottom	has	a	porous	plug	which	allows	
the	gas	inert	argon	supply.	
Moreover	 the	 LF	 stand	 is	 also	 equipped	 with	 an	 addition	 hopper	 mounted	 on	 the	 cover	
(ferroalloys	addition)	and	a	lance	for	injection	of	desulfurizing	agent.	
During	the	treatment,	molten	steel	is	covered	by	a	layer	of	slag.	The	fumes	formed	during	the	
operation	are	extracted	through	a	suction	system	installed	at	the	cover.
23	
	
Additional	devices,	such	as	
VD	(vacuum	degasser)	could	
be	adopted	in	the	secondary	
metallurgy	in	order	to	
produce	special	kind	of	steel.
24	
CONTINUOUS	CASTING
The	 molten	metal	 is	 now	cast	
through	 a	 mold,	 the	 casting	
takes	 the	 two	 dimensional	
profile	 of	 the	 mold	 but	 its	
length	 is	 indeterminate.	 The	
casting	 will	 keep	 traveling	
downward	 and	 its	 length	
increases	 with	 time.	 New	
molten	 steel	 is	 constantly	
supplied	 to	 the	 mold	 with	 a	
specific	 rate	 to	 keep	 up	 with	
the	solidifying	casting.
25	
Molten	metal,	from	the	ladle,	is	poured	into	a	tundish,	which	is	a	container	that	is	located	
above	the	mold,	it	holds	the	liquid	metal	for	the	casting.	This	particular	casting	operation	
uses	 the	 force	 of	 gravity	 to	 fill	 the	 mold	 and	 to	 help	 move	 along	 the	 continuous	 metal	
casting.	The	tundish	is	constantly	supplied	with	molten	steel	to	keep	the	process	going.	The	
whole	 process	 is	 controlled	 to	 ensure	 there	 is	 smooth	 flow	 of	 molten	 steel	 through	
tundish.	
Further,	the	impurities	and	slag	are	filtered	in	tundish	before	they	move	into	the	mold.	The	
entrance	of	the	mold	is	filled	with	inert	gases	to	prevent	reaction	of	molten	steel	with	the	
gases	in	the	environment	like	oxygen.	The	molten	metal	moves	swiftly	through	the	mold	
and	it	does	not	completely	solidify	in	it.	The	entire	mold	is	cooled	with	water	that	flows	
along	the	outer	surface.	
The	metal	casting	moves	outside	the	mold	with	the	help	of	different	sets	of	rollers.	While	
one	set	of	rollers	bend	the	metal	cast,	another	set	will	straighten	it.	This	helps	to	change	
the	direction	of	flow	of	the	steel	slab	from	vertical	to	horizontal.

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