ALBERTUS SEPTYANTOKO 
2712100014
IRON ORE 
• Iron = 65-67 % 
• SiO2 + Al2O3 = 2-3 % 
• CaO + MgO = 0,5-1 % 
• Sulphur = 0,02 % max 
• Phosphorus = 0,04 % max 
Chemical 
Composition 
• Size = 5-18 mm 
• Shatter Index = +95 % 
• Tumbler index = +88 % 
• Reducibility Index = +94 % 
• Thermal Degradation Index = 5 
% 
Physical 
Composition
COAL 
• Fixed Carbon = 45 % 
• Volatile Matter = 25-30 % 
• Ash = 20 % 
• Moisture = 8 % 
Chemical 
Composition 
• Size = 3-20 mm 
Physical 
Composition
DOLOMITE 
• MgO = 20 % 
• CaO = 28 % min 
• SiO2= 5 % max 
Chemical 
Composition 
• Size = 2-6 mm Physical 
Composition
PRIMARY AIR 
Primary air is used to combustion the injection 
coal 
Temperature in used below 950 C
SECONDARY AIR 
Secondary air is introduced axially in the direction of the 
gas flow 
The air supplied to the length of the kiln is metered for 
close control of temperature and gas atmosphere in the 
kiln 
Heating zone extends from 25% to 40% along length of 
the kiln and in the reduction zone
INJECTION COAL 
Coal Crushing Combustion 
Injection to 
kiln 
Coal Injection over a large range of size 0-20 mm 
Temperature combustion below 950 C 
Coal injection system makes use of voal volatiles for reduction, 
thereby reducing the coal requirement to a minimum 
Coal Injection can decrease energy consumption
ROTARY KILN
ROTARY KILN
ROTARY COOLER 
The product come to the water cooled 
Where its temperature reaches to 80-100 C
ROTARY COOLER 
The product is conveyed to the product separation 
and storage building 
The product is Sponge iron and char 
Place that spraying a controlled amount of water directly 
into hot solids and by spraying additional water outside the 
cooler shell
SCREENING 
+ 10 mm 3-10 mm - 3 mm
MAGNETIC SEPARATOR 
+ 10 mm 3-10 mm - 3 mm 
Mag. pulley 
Mag. 
separation 
Mag. 
separation
MAGNETIC SEPARATOR 
+ 10 mm 
3-10 mm 
waste 
Sponge iron 
Lumps + 
char 
Sponge iron 
Lumps + 
3-10 mm magnetic + Non magnetic 
char 
Sponge iron 
Lumps + char
SPONGE IRON 
• Fe (T)= 91,5 % min 
• Fe (M) = 85,5 % min 
• Sulphur = 0,005 % 
• Phosphorus = 0,7 % 
Chemical 
Composition 
• Size = -3 to 10 mm 
• Bulk density=1,7-2T/M3 
Physical 
Composition
POST COMBUSTION CHUMBER 
To maintain temperature in rotary Kiln 
Press particles in flame gas
WASTE HEAT RECOVERY BOILER 
Cultivate waste heat temperature is produced of 
combustion to produce steam to electricty 
generation 
This steam is channeled to ESP and turbine
ELECTRO STATIC PRECIPITATOR 
Clean gas from WHRB. Gas is sent to stack 
Turbine cultivate steam to electricty generation
Sponge iron making process

Sponge iron making process

  • 1.
  • 3.
    IRON ORE •Iron = 65-67 % • SiO2 + Al2O3 = 2-3 % • CaO + MgO = 0,5-1 % • Sulphur = 0,02 % max • Phosphorus = 0,04 % max Chemical Composition • Size = 5-18 mm • Shatter Index = +95 % • Tumbler index = +88 % • Reducibility Index = +94 % • Thermal Degradation Index = 5 % Physical Composition
  • 4.
    COAL • FixedCarbon = 45 % • Volatile Matter = 25-30 % • Ash = 20 % • Moisture = 8 % Chemical Composition • Size = 3-20 mm Physical Composition
  • 5.
    DOLOMITE • MgO= 20 % • CaO = 28 % min • SiO2= 5 % max Chemical Composition • Size = 2-6 mm Physical Composition
  • 6.
    PRIMARY AIR Primaryair is used to combustion the injection coal Temperature in used below 950 C
  • 7.
    SECONDARY AIR Secondaryair is introduced axially in the direction of the gas flow The air supplied to the length of the kiln is metered for close control of temperature and gas atmosphere in the kiln Heating zone extends from 25% to 40% along length of the kiln and in the reduction zone
  • 8.
    INJECTION COAL CoalCrushing Combustion Injection to kiln Coal Injection over a large range of size 0-20 mm Temperature combustion below 950 C Coal injection system makes use of voal volatiles for reduction, thereby reducing the coal requirement to a minimum Coal Injection can decrease energy consumption
  • 9.
  • 10.
  • 11.
    ROTARY COOLER Theproduct come to the water cooled Where its temperature reaches to 80-100 C
  • 12.
    ROTARY COOLER Theproduct is conveyed to the product separation and storage building The product is Sponge iron and char Place that spraying a controlled amount of water directly into hot solids and by spraying additional water outside the cooler shell
  • 13.
    SCREENING + 10mm 3-10 mm - 3 mm
  • 14.
    MAGNETIC SEPARATOR +10 mm 3-10 mm - 3 mm Mag. pulley Mag. separation Mag. separation
  • 15.
    MAGNETIC SEPARATOR +10 mm 3-10 mm waste Sponge iron Lumps + char Sponge iron Lumps + 3-10 mm magnetic + Non magnetic char Sponge iron Lumps + char
  • 16.
    SPONGE IRON •Fe (T)= 91,5 % min • Fe (M) = 85,5 % min • Sulphur = 0,005 % • Phosphorus = 0,7 % Chemical Composition • Size = -3 to 10 mm • Bulk density=1,7-2T/M3 Physical Composition
  • 17.
    POST COMBUSTION CHUMBER To maintain temperature in rotary Kiln Press particles in flame gas
  • 18.
    WASTE HEAT RECOVERYBOILER Cultivate waste heat temperature is produced of combustion to produce steam to electricty generation This steam is channeled to ESP and turbine
  • 19.
    ELECTRO STATIC PRECIPITATOR Clean gas from WHRB. Gas is sent to stack Turbine cultivate steam to electricty generation