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TUTORIAL
on
ROASTING FURNACES
Prepared
By
Mr.. Sunil D. Kahar
Assistant Professor
Metallurgical & Materials Engineering Department
Faculty of Technology & Engineering
The M S University of Baroda, Vadodara
Roasting
- Minerals or constituent of ore other chemical form
 Oxidizing Roasting
- Metal sulphide Metal oxide
MS + 3/2 O2 MO + SO2
 Volatizing Roasting
- Elimination of volatile oxide such as AS2O3, Sb2O3, ZnO
 Chloridizing Roasting
- Metal compound chloride under oxidizing or reducing condition
2NaCl + MS +2O2 Na2SO4 + MCl2
2NaCl + 2MO +S2 + 3O2 Na2SO4 + 2 MCl2
- ( U, Be, Nb, Zr, Ti extracted from there oxides)
O2 or heating
 Sulphatizing Roasting
- Sulphide sulphates prior to leaching
 Magnetic Roasting
- Controlled reduction of hematite (Fe2O3 ) magnetite (Fe3O4)
 Reduction Roasting
- Partial reduction of an oxide ore prior to actual reduction smelting
 Blast Roasting or Sinter Roasting
- Partial oxidized as well as physical conditioned ore is charge.
 Roasting depend upon
1. Time
2. Temperature
3. Avaibility of O2 or air
4. physical condition nature of the mechanical device
 Criteria of selection of roasting process
1. Physical condition of product
blast furnace smelting – product should coarse or cellular
reverberatory furnace – product should ne fine
leaching - product should be porous
2. Chemical composition of product
For copper – retain some sulphur
For Lead & Zinc - complete elimination of sulphur
Multiple Hearth Roaster
MacDougall in England (19th Centaury)
Basic principle - Counter current flow of
solid ore & the oxidizing gases
- diameter = 25 ft, 6 to 12 hearth
- Steel shell lined with cylindrical brick
- Ore is charge from top
- Revolving mechanical rabble attach to
arm
– continuously shifting the ore
- Arm is attach with rotating shaft
- Oxidizing gases move upward
- External heating of charge is unnecessary
except when charge content moisture
Drawbacks:
(1) Roasting is slow
(2) Gases are unsuitable for production of
H2SO4
Fluidizing Bed Roasting
Principle-
-Ore particles are roasted while it is
suspended in an upward stream of
gases
-Gas is passes through the bottom of the
bed
- Behahaviour bed depend on the
velocity of gas
Stage-1
• Bed is porous - gas easily flow
• Pressure drop across the bed
– proportional to flow rate
• Factor influencing the flow rate
1. Void fraction
2. Particle size factor
3. Particle shape factor
Stage-2
• Gas velocity is with expand of the bed in
upward direction due to drag force
exerted by gas stream
Stage-3
• Continue to gas velocity
• Presuure drop = wt. of the particle per unit
area of bed
So particle offer less resistance to gas flow
• Stage-4
• Further increase in gas velocity lead to
continued expansion of the bed
• Result in increase in inter particle distance
• Pressure drop across bed is decrease with
increase in gas velocity
• Stage-5
• expansion of the bed is independent of gas
velocity
• Out coming gas appear as babble & bursting on
the surface of the bed
• Look like well stirred boiling liquid –said to be
fluidized.
Flash Roaster
• Preheated ore – free fall through body of hot air
• Instantaneous oxidation of flashing of combustible constituent ore( S)
• Hence called flash roasting
• Ore should be in fine form
• Capacity pf flash roaster > hearth roaster
• Temp. pf combustion zone = 900-9500 C
Sinter Roasting OR Blast Roasting
• Fine ore & concentrate have been
agglomerated before charging
• Use for Sulphides ore
• 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 discharge
• Produce porous cinder called sinter
• Cooled sinter is sized ti give uniform
product

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Tutorial on roasting furnaces s.d.kahar

  • 1. TUTORIAL on ROASTING FURNACES Prepared By Mr.. Sunil D. Kahar Assistant Professor Metallurgical & Materials Engineering Department Faculty of Technology & Engineering The M S University of Baroda, Vadodara
  • 2. Roasting - Minerals or constituent of ore other chemical form  Oxidizing Roasting - Metal sulphide Metal oxide MS + 3/2 O2 MO + SO2  Volatizing Roasting - Elimination of volatile oxide such as AS2O3, Sb2O3, ZnO  Chloridizing Roasting - Metal compound chloride under oxidizing or reducing condition 2NaCl + MS +2O2 Na2SO4 + MCl2 2NaCl + 2MO +S2 + 3O2 Na2SO4 + 2 MCl2 - ( U, Be, Nb, Zr, Ti extracted from there oxides) O2 or heating
  • 3.  Sulphatizing Roasting - Sulphide sulphates prior to leaching  Magnetic Roasting - Controlled reduction of hematite (Fe2O3 ) magnetite (Fe3O4)  Reduction Roasting - Partial reduction of an oxide ore prior to actual reduction smelting  Blast Roasting or Sinter Roasting - Partial oxidized as well as physical conditioned ore is charge.
  • 4.  Roasting depend upon 1. Time 2. Temperature 3. Avaibility of O2 or air 4. physical condition nature of the mechanical device  Criteria of selection of roasting process 1. Physical condition of product blast furnace smelting – product should coarse or cellular reverberatory furnace – product should ne fine leaching - product should be porous 2. Chemical composition of product For copper – retain some sulphur For Lead & Zinc - complete elimination of sulphur
  • 5. Multiple Hearth Roaster MacDougall in England (19th Centaury) Basic principle - Counter current flow of solid ore & the oxidizing gases - diameter = 25 ft, 6 to 12 hearth - Steel shell lined with cylindrical brick - Ore is charge from top - Revolving mechanical rabble attach to arm – continuously shifting the ore - Arm is attach with rotating shaft - Oxidizing gases move upward - External heating of charge is unnecessary except when charge content moisture Drawbacks: (1) Roasting is slow (2) Gases are unsuitable for production of H2SO4
  • 6. Fluidizing Bed Roasting Principle- -Ore particles are roasted while it is suspended in an upward stream of gases -Gas is passes through the bottom of the bed - Behahaviour bed depend on the velocity of gas
  • 7. Stage-1 • Bed is porous - gas easily flow • Pressure drop across the bed – proportional to flow rate • Factor influencing the flow rate 1. Void fraction 2. Particle size factor 3. Particle shape factor Stage-2 • Gas velocity is with expand of the bed in upward direction due to drag force exerted by gas stream Stage-3 • Continue to gas velocity • Presuure drop = wt. of the particle per unit area of bed So particle offer less resistance to gas flow
  • 8. • Stage-4 • Further increase in gas velocity lead to continued expansion of the bed • Result in increase in inter particle distance • Pressure drop across bed is decrease with increase in gas velocity • Stage-5 • expansion of the bed is independent of gas velocity • Out coming gas appear as babble & bursting on the surface of the bed • Look like well stirred boiling liquid –said to be fluidized.
  • 9. Flash Roaster • Preheated ore – free fall through body of hot air • Instantaneous oxidation of flashing of combustible constituent ore( S) • Hence called flash roasting • Ore should be in fine form • Capacity pf flash roaster > hearth roaster • Temp. pf combustion zone = 900-9500 C
  • 10. Sinter Roasting OR Blast Roasting • Fine ore & concentrate have been agglomerated before charging • Use for Sulphides ore • 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 discharge • Produce porous cinder called sinter • Cooled sinter is sized ti give uniform product