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Principles of Roasting and Its 
Types 
By: AKSHAT CHATURVEDI 
ANITA KASOT 
HEENA YADAV 
HITESH GUPTA 
MUKESH NAINWAL 
PRACHI BAFNA
Various Metallurgical 
Proceses 
 Hydrometallurgy is a method for obtaining metals from their 
ores. It is a technique within the field of extractive 
metallurgy involving the use of aqueous chemistry for the 
recovery of metals from ores, concentrates, and recycled or 
residual materials 
 Electrometallurgy is a term used for processes that refine or 
purify metals using electricity. It can also be a general term for 
electrical processes used to plate one metal with another for 
decorative or corrosion resistance purposes. 
 Pyrometallurgy is a branch of extractive metallurgy. It 
consists of the thermal treatment of minerals and 
metallurgical ores and concentrates to bring about physical 
and chemical transformations in the materials to enable 
recovery of valuable metals
Pyrometallurgy 
 Pyrometallurgy deals with the extraction of 
minerals from ore by treating them with heat. 
Pyrometallurgy 
Calcination Roasting Smelting
ROASTING 
 In roasting, the ore is heated in a regular supply of air in 
a furnace at a temperature below the melting point of 
the metal. 
 Roasting is a metallurgical process involving gas–solid 
reactions at elevated temperatures with the goal of 
purifying the metal component(s). 
 Often before roasting, the ore has already been partially 
purified, e.g. by froth floatation. The concentrate is 
mixed with other materials to facilitate the process. 
 This process is generally applied to sulphide minerals. 
During roasting, the sulfide is converted to an oxide, 
and sulfur is released as sulfur dioxide, a gas.
 For the ores Cu2S (chalcocite) and ZnS 
(sphalerite), balanced equations for the roasting 
are:- 
 2 Cu2S + 3O2 → 2 Cu2O + 2 SO2 
2 ZnS + 3 O2 → 2 ZnO + 2 SO2
PROCESSES 
There are several different types of roast, each one 
intended to produce a specific reaction and to yield a 
roasted product (or calcine) suitable for the particular 
processing operation to follow. The roasting 
procedures are: 
 Oxidizing roasts - which remove all or part of the 
sulfur from sulfide metal compounds, replacing the 
sulfides with oxides. (The sulfur removed goes off 
as sulfur dioxide gas.) Oxidizing roasts are 
exothermic. 
 Sulfatizing roasts - which convert certain metals 
from sulfides to sulfates. Sulfatizing roasts are 
exothermic.
 Reducing roasts, which lower the oxide state 
or even completely reduce an oxide to a metal. 
Reducing roasts are exothermic. 
 Chloridizing roasts, or chlorination, which 
change metallic oxides to chlorides by heating 
with a chlorine source such as chlorine gas, 
hydrochloric acid gas, ammonium chloride, or 
sodium chloride. These reactions are 
exothermic. 
 Volatilizing roasts, which eliminate easily 
volatilized oxides by converting them to gases. 
 Calcination, in which solid material is heated to 
drive off either carbon dioxide or chemically 
combined water. Calcination is an endothermic 
reaction.
Roasting depends on following factors: 
1. Time 
2. Temperature 
3. Avaibility of O2 or air 
4. Physical condition 
 Criteria of selection of roasting process 
1. Physical condition of product blast furnace 
smelting product should coarse or cellular 
reverberatory furnace – product should be fine 
leaching – product should be porous . 
2. Chemical composition of product 
For copper – retain some sulphur 
For Lead & Zinc - complete elimination of 
sulphur .
ROASTERS 
 Each of the above processes can be carried out in 
specialized roasters. 
 The types most commonly in use are fluidized-bed, 
multiple-hearth, flash, chlorinator, rotary kiln, 
and sintering machine (or blast roaster).
Flash Roasting 
 Preheated ore particles are made to fall through 
body of hot air resulting in 
 Instantaneous oxidation or ‘flashing’ of combustible 
constituents of the ore, mainly sulphur 
 Hence called flash roasting 
 Ore should be of fine size 
 Capacity of flash roaster > hearth roaster 
 Temp. of combustion zone = 900-9500 C
Sinter Roasting/Blast 
Roasting 
 Fine ore & concentrate have to be agglomerated 
before they can be charged in a blast furnace 
 Treatment of sulphide ore in a sintering machine 
where roasting and agglomeration take place 
simultaneously 
 Charge = (fine ore+ moisture) as layer of 15-50 cm 
thick on revolving belt 
 Combustion is done by burner 
 Speed is adjusted - roasting should be completed 
before it is discharged 
 Produce porous cinder called sinter 
 Cooled sinter is sized to give uniform product
Multiple Hearth Roasting 
Basic principle – 
Counter current flow of solid ore & the oxidizing 
gases. 
Working: 
- The hearth at the top dry and heat the charge 
- Ore is discharged automatically at the top hearth 
- It gradually moves downwards through alternate 
passages around the shaft and periphery and 
finally emerges at the bottom 
- The oxidizing gases flow upwards 
- External heating of charge is unnecessary 
except when charge contain moisture
Drawbacks : 
(1) Roasting is slow 
(2) Gases are unsuitable for production of H2SO4 
because they do not contain sufficient SO2 and 
SO3 
Pictorial view of multiple hearth roasting unit
Sintering Machine
Fluidized-bed roasting 
Principle- 
- Ore particles are roasted 
while it is suspended in an 
upward stream of gases 
- Gas passes through 
bottom of the bed 
- Behahaviour of the bed 
depends on the velocity of 
gas
Fluidized-bed roasting 
 The ore particles are roasted while suspended in 
an upward stream of gas 
 Finely ground sulfide concentrates in size over the 
range 0.005 to 0.05 cm in diameter is used 
 As in the suspension roaster, the reaction rates for 
desulfurization are more rapid than in the older 
multiple-hearth processes. 
 Fluidized-bed roasters operate under a pressure 
slightly lower than atmospheric and at 
temperatures averaging 1000°C (1800°F). 
 In the fluidized-bed process, no additional fuel is 
required after ignition has been achieved.
Steps observed during roasting 
process 
Stage-1 
 When the gas flow rate is very low, and the ore 
bed is porous, the gas permeates the bed 
without disturbing the ore particles 
 Pressure drop across the bed is proportional to 
flow rate 
Stage-2 
 Gas velocity increses, the bed expands 
upwards due to the effect of the drag forces 
exerted by gas stream 
 The pressure drop across the bed depends on 
the gas velocity
Stage-3 
 When gas velocity further increases a stage is 
reached 
 Pressure drop = wt. of the particle per unit area of 
the bed 
 Particles remain individually suspended and offer 
less resistance to gas flow 
Stage-4 
 Further increase in gas velocity lead to continued 
expansion of the bed 
 Results in increase in interparticle distance 
 Pressure drop across bed continues to decrease 
as the gas velocity increases
Stage-5 
 Finally, the expansion of the bed is independent of 
gas velocity 
 Outcoming gas stream appears in the form of 
bubbles bursting on the surface of the bed which 
looks like well stirred boiling liquid 
 In this condition the bed is said to be fluidized. 
 The fluidized bed has an apparent density distinctly 
different from the density of the solid and is 
capable of flowing like a liquid.
The Fluidization Behaviour
Advantages 
 High energy efficiency because it can 
be autogenously operated 
 Useful in recovery of sulphur because 
the gas that it produces has high SO2 
content 
 Ideal for roasting of oxide ores 
because the oxidizing reactions that 
take place during roasting is highly 
exothermic. 
e.g. Pyrite FeS2, Millerite NiS, etc.
Any queries 
…..??????

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Principals of roasting and its types

  • 1. Principles of Roasting and Its Types By: AKSHAT CHATURVEDI ANITA KASOT HEENA YADAV HITESH GUPTA MUKESH NAINWAL PRACHI BAFNA
  • 2. Various Metallurgical Proceses  Hydrometallurgy is a method for obtaining metals from their ores. It is a technique within the field of extractive metallurgy involving the use of aqueous chemistry for the recovery of metals from ores, concentrates, and recycled or residual materials  Electrometallurgy is a term used for processes that refine or purify metals using electricity. It can also be a general term for electrical processes used to plate one metal with another for decorative or corrosion resistance purposes.  Pyrometallurgy is a branch of extractive metallurgy. It consists of the thermal treatment of minerals and metallurgical ores and concentrates to bring about physical and chemical transformations in the materials to enable recovery of valuable metals
  • 3. Pyrometallurgy  Pyrometallurgy deals with the extraction of minerals from ore by treating them with heat. Pyrometallurgy Calcination Roasting Smelting
  • 4. ROASTING  In roasting, the ore is heated in a regular supply of air in a furnace at a temperature below the melting point of the metal.  Roasting is a metallurgical process involving gas–solid reactions at elevated temperatures with the goal of purifying the metal component(s).  Often before roasting, the ore has already been partially purified, e.g. by froth floatation. The concentrate is mixed with other materials to facilitate the process.  This process is generally applied to sulphide minerals. During roasting, the sulfide is converted to an oxide, and sulfur is released as sulfur dioxide, a gas.
  • 5.  For the ores Cu2S (chalcocite) and ZnS (sphalerite), balanced equations for the roasting are:-  2 Cu2S + 3O2 → 2 Cu2O + 2 SO2 2 ZnS + 3 O2 → 2 ZnO + 2 SO2
  • 6. PROCESSES There are several different types of roast, each one intended to produce a specific reaction and to yield a roasted product (or calcine) suitable for the particular processing operation to follow. The roasting procedures are:  Oxidizing roasts - which remove all or part of the sulfur from sulfide metal compounds, replacing the sulfides with oxides. (The sulfur removed goes off as sulfur dioxide gas.) Oxidizing roasts are exothermic.  Sulfatizing roasts - which convert certain metals from sulfides to sulfates. Sulfatizing roasts are exothermic.
  • 7.  Reducing roasts, which lower the oxide state or even completely reduce an oxide to a metal. Reducing roasts are exothermic.  Chloridizing roasts, or chlorination, which change metallic oxides to chlorides by heating with a chlorine source such as chlorine gas, hydrochloric acid gas, ammonium chloride, or sodium chloride. These reactions are exothermic.  Volatilizing roasts, which eliminate easily volatilized oxides by converting them to gases.  Calcination, in which solid material is heated to drive off either carbon dioxide or chemically combined water. Calcination is an endothermic reaction.
  • 8. Roasting depends on following factors: 1. Time 2. Temperature 3. Avaibility of O2 or air 4. Physical condition  Criteria of selection of roasting process 1. Physical condition of product blast furnace smelting product should coarse or cellular reverberatory furnace – product should be fine leaching – product should be porous . 2. Chemical composition of product For copper – retain some sulphur For Lead & Zinc - complete elimination of sulphur .
  • 9. ROASTERS  Each of the above processes can be carried out in specialized roasters.  The types most commonly in use are fluidized-bed, multiple-hearth, flash, chlorinator, rotary kiln, and sintering machine (or blast roaster).
  • 10. Flash Roasting  Preheated ore particles are made to fall through body of hot air resulting in  Instantaneous oxidation or ‘flashing’ of combustible constituents of the ore, mainly sulphur  Hence called flash roasting  Ore should be of fine size  Capacity of flash roaster > hearth roaster  Temp. of combustion zone = 900-9500 C
  • 11. Sinter Roasting/Blast Roasting  Fine ore & concentrate have to be agglomerated before they can be charged in a blast furnace  Treatment of sulphide ore in a sintering machine where roasting and agglomeration take place simultaneously  Charge = (fine ore+ moisture) as layer of 15-50 cm thick on revolving belt  Combustion is done by burner  Speed is adjusted - roasting should be completed before it is discharged  Produce porous cinder called sinter  Cooled sinter is sized to give uniform product
  • 12. Multiple Hearth Roasting Basic principle – Counter current flow of solid ore & the oxidizing gases. Working: - The hearth at the top dry and heat the charge - Ore is discharged automatically at the top hearth - It gradually moves downwards through alternate passages around the shaft and periphery and finally emerges at the bottom - The oxidizing gases flow upwards - External heating of charge is unnecessary except when charge contain moisture
  • 13. Drawbacks : (1) Roasting is slow (2) Gases are unsuitable for production of H2SO4 because they do not contain sufficient SO2 and SO3 Pictorial view of multiple hearth roasting unit
  • 15. Fluidized-bed roasting Principle- - Ore particles are roasted while it is suspended in an upward stream of gases - Gas passes through bottom of the bed - Behahaviour of the bed depends on the velocity of gas
  • 16. Fluidized-bed roasting  The ore particles are roasted while suspended in an upward stream of gas  Finely ground sulfide concentrates in size over the range 0.005 to 0.05 cm in diameter is used  As in the suspension roaster, the reaction rates for desulfurization are more rapid than in the older multiple-hearth processes.  Fluidized-bed roasters operate under a pressure slightly lower than atmospheric and at temperatures averaging 1000°C (1800°F).  In the fluidized-bed process, no additional fuel is required after ignition has been achieved.
  • 17. Steps observed during roasting process Stage-1  When the gas flow rate is very low, and the ore bed is porous, the gas permeates the bed without disturbing the ore particles  Pressure drop across the bed is proportional to flow rate Stage-2  Gas velocity increses, the bed expands upwards due to the effect of the drag forces exerted by gas stream  The pressure drop across the bed depends on the gas velocity
  • 18. Stage-3  When gas velocity further increases a stage is reached  Pressure drop = wt. of the particle per unit area of the bed  Particles remain individually suspended and offer less resistance to gas flow Stage-4  Further increase in gas velocity lead to continued expansion of the bed  Results in increase in interparticle distance  Pressure drop across bed continues to decrease as the gas velocity increases
  • 19. Stage-5  Finally, the expansion of the bed is independent of gas velocity  Outcoming gas stream appears in the form of bubbles bursting on the surface of the bed which looks like well stirred boiling liquid  In this condition the bed is said to be fluidized.  The fluidized bed has an apparent density distinctly different from the density of the solid and is capable of flowing like a liquid.
  • 21. Advantages  High energy efficiency because it can be autogenously operated  Useful in recovery of sulphur because the gas that it produces has high SO2 content  Ideal for roasting of oxide ores because the oxidizing reactions that take place during roasting is highly exothermic. e.g. Pyrite FeS2, Millerite NiS, etc.
  • 22.