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Extraction of Mg
Department of MME
Extraction of Non-Ferrous Metals
Details about of Mg
Atomic Number: 12
Atomic Weight: 24 amu
Density: 1.738 gm/cm 3
Melting Point: 6500 C
Boiling Point: 1107 0C
Common Minerals of Mg
Dolomite – MgCO3.CaCO3
Magnesite – MgCO3
MgCl2 and MgSO4 present in sea water
Brucite- [Mg(OH)2]
Carnallite- (MgCl2.KCl.6H2O)
Olivine- (Mg2SiO4)
Serpentine- (Mg3Si2O7)
Asbestos – (CaSiO3.3MgSiO3)
Kainite- (MgSO4.KCl.3H2O)
 Dolomite and magnesite are commercial minerals.
 Magnesium hydroxide derived from sea water have sufficiently high Mg content sand do not
require upgradation before subsequent extraction.
Problems encountered during the extraction of Mg by
Pyrometallurgical process
MgO is very stable oxide and requires T>1800℃ for
carbothermic reduction.
Such high temp. is not practicable with external
heating.
Reduction temp. can be reduce by using vacuum to
distil off the Mg and to drive the reduction reaction in
forward direction.
𝑀𝑔𝑂 𝑐 + 𝐶 𝑐 ↔ 𝑀𝑔 𝑔 + 𝐶𝑂(𝑔)
However, it is very difficult to prevent the backward
reaction, and hence carbothermic reduction has not
commercially accepted.
Reduction of MgO by other reductants like CaC2 and
Al at 1200℃ under vacuum is feasible, but not
commercially attractive.
𝑀𝑔𝑂 𝑐 + 𝐶𝑎𝐶2 𝑐 → 𝐶𝑎𝑂 𝑐 + 𝑀𝑔 𝑔 + 2𝐶
3𝑀𝑔𝑂 𝑐 + 2𝐴𝑙 𝑙 → 𝐴𝑙2 𝑂3 𝑐 + 3𝑀𝑔 (𝑔)
Problems encountered in Electrometallurgy viz. direct
electrolysis from aqueous medium
Mg requires 2.3V more than H2 for deposition and the hydrogen overvoltage is not
sufficiently high to overcome this voltage hydrogen is evolved before magnesium can
be deposited.
To generate sufficiently high hydrogen overvoltage, amalgam cathode can be employed.
It can serve two (2) purposes:
1. Because of its extremely smooth surface, hydrogen overvoltage is rendered difficult.
2. The low activity of Mg in amalgam cathode lowers the Mg deposition potential.
However, amalgam cathode has not found commercially acceptable.
Extraction of Mg by Pyrometallurgical process
PIDGEON Process
Thermodynamically pure Si can not reduce MgO when both reactant and products are in their standard state.
Therefore, the Pidgeon process reduces pressure to remove the Mg vapor and drive the reduction process. In
this process, calsined dolomite is briquetted with powered ferrosilicon (75% Si), and the reduction is carried
out under vacuum of 0.1 mm Hg at 1100-1200℃ in an externally heated retort.
𝟐𝑴𝒈𝑶. 𝑪𝒂𝑶 𝒄 + 𝑭𝒆𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝟐𝑪𝒂𝑶. 𝑺𝒊𝑶 𝟐 𝒄 + 𝑭𝒆 (𝒄) ………. (1)
Since Mg is the only, it can be easily removed from the reaction chamber to avoid possibility of backward
reaction.
Presence of CaO lowers the free energy of the reduction reaction. The free energies of the reactions at
1200℃:
𝟐𝑴𝒈𝑶 + 𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝑺𝒊𝑶 𝟐 𝒄 ∆𝑮 𝟎 = 𝟓𝟐 𝒌𝒄𝒂𝒍, ∆𝑯 𝟎 = 𝟏𝟑𝟔 𝒌𝒄𝒂𝒍 …….. (2)
𝟐𝑴𝒈𝑶 + 𝟐𝑪𝒂𝑶 𝒄 + 𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝟐𝑪𝒂𝑶. 𝑺𝒊𝑶 𝟐 𝒄 𝑮 𝟎 = 𝟏𝟗 𝒌𝒄𝒂𝒍, ∆𝑯 𝟎 = 𝟏𝟏𝟐 𝒌𝒄𝒂𝒍…(3)
At 1200℃ the equilibrium pressure of Mg for reaction (3) is 15 mm Hg, and to attain 1 atm. of Mg about
1700℃ is required. Such high temp. is not practicable with external heating, therefore, Pidgeon process
incorporates vacuum to drive the reaction (3) in forward direction.
Reaction (6) is highly endothermic. Addition of CaF2 and MgF2 acts as catalyst and speeds up the evolution
of Mg vapor.
PIDGEON Process (continue..)
PIDGEON Process (continue..)
Reaction Mechanism:
The reaction occurs through transient liquid phase at some intermediate stages. Distinct stages of Pidgeon
process are:
(1) The initial reaction between CaO and Fe-Si produce liquid Ca-Si-Fe alloy, which permeates the briquette
and forms a metallic network. The reaction occur at around1000℃ and mildly exothermic. The ternary
alloy serves as the main reducing agent.
(2) Mg vapors produce by reduction of MgO by Ca-Si-Fe alloy. At this stage, pressure increases rapidly and
slows down the rate of reaction. Te subsequent reaction rate is governed by the rate at which Mg can escape
from the briquettes.
Kinetics of the reaction controlled by the presence of SiO vapor in Pidgeon process as:
𝑀𝑔𝑂 (c) +𝑆𝑖 (c) →𝑀𝑔 (g) +𝑆𝑖𝑂 (g)
2𝑆𝑖𝑂 (g)+2𝐶𝑎𝑂 (c) →2𝐶𝑎𝑂.𝑆𝑖𝑂2 (c) +𝑆𝑖 (c)
MAGNETOTHERM Process
It is essentially a ferrosilicon reduction process carried out at 1500℃ and the bath is
maintained in molten state by the addition of aluminum to form a molten slag.
DOW Process: Extraction of Mg from Sea-Water
DOW Process: Flow Chart
DOW Process: Flow Chart Explanation
Developed by the Dow Chemical Company (U.S.A).
It involves the collection of Mg as insoluble hydroxide by precipitation with lime as:
𝑀𝑔𝐶𝑙2 + 𝐶𝑎(𝑂𝐻)2→ 𝑀𝑔(𝑂𝐻)2+𝐶𝑎𝐶𝑙2
𝑀𝑔𝑆𝑂4 + 𝐶𝑎(𝑂𝐻)2= 𝑀𝑔(𝑂𝐻)2= 𝐶𝑎𝑆𝑂4
The suspension is distributed to thickeners, in which the hydroxide settle and the cleaner overflow
pumped back to the sea.
The milk of magnesia (slurry) underflow is pumped to filter tank, and subsequently agitated with
10% HCl, which converts it to a weak solution of chloride. This dilute solution is concentrated and
filtered to recover the crystallized solids.
The filtrate is then subjected to evaporation to recover remaining chloride. Evaporation is
carefully controlled as the hydrous chloride is liable to lose hydrogen chloride, which results in
oxide contamination in the final product. The reaction is:
𝑀𝑔𝐶𝑙2. 6𝐻2 𝑂 = 𝑀𝑔𝑂 + 2𝐻𝐶𝑙 + 5𝐻2 𝑂
DOW Process: Flow Chart Explanation
Electrolysis of Magnesium Chloride:
Principle:
Mg is reactive metal, has a high decomposition potential. Therefore, during aqueous electrolysis
hydrogen evolution occurs before the decomposition of MgCl2Not feasible
For electrolysis of MgCl2, the electrolyte is normally composed of 25-30% MgCl2, 15% CaCl2 and
50-60% NaCl. A large amount of flux is necessary to maintain fluidity and to increase the density of
the bath so that the liberated metal at cathode floats on the surface of the electrolyte. The theoretical
decomposition voltage of dissolved MgCl2 is 3.3, but the resistance of the bath raises the voltage to
6.6. A current of 30,000-50,000 A is employed and the temperature of the electrolytic cell is
maintained at 670-730℃.
Cell design:
The electrolytic cell for Mg extraction may be divided into two (2) categories: lined and unlined.
Unlined cell must be provided with separate cathodes, usually made of steel, whereas in case of
unlined cell, the steel wall of the cell itself may be used as cathode. Graphite anode is used for both
cell. The anodes are inert, therefore, not consumed. The cell operate in an inert atmosphere.
DOW Process: Flow Chart Explanation
It is necessary to prevent chlorination of metallic
product by gaseous choline evolved at the anode. Thus,
the metal must be diverted away from the anode zone
and recombination prevented by special design features.
Cl gas is collected in a special hood and the collection
of the metal is facilitated by diverting to a pool. The
chlorine set free at the anode is used to dry the
incoming MgCl2 and also to chlorinate Mg(OH)2.
However, complete drying is both expensive and
difficult. Therefore, for electrolyzing a chloride that has
been one and two moles of combined water have been
evolved.
Uses or Applications of Mg
Magnesium
Non-structural
Uses
Alloying De-oxidation and
De-sulphurization
Modifying
structure of
graphite in cast
iron
Pyrotechnics
and
Photography
Cathodic
protection
structural
Uses
Uses or Applications of Mg
Nonstructural uses:
1. Alloying: Mg is widely used in alloying, especially in Al-Based alloys, to improve strength,
hardness and corrosion resistance. It also improves mechanical properties of Pb-based alloys
containing Ca, Sn and In.
2. Deoxidation and desulphurization: Mg has strong affinity for oxygen, effectively deoxidizes
many molten metals. For production of iron and steel, the S content in the BF coke is rather high,
and the pig iron contains a large quantity of S. To reduce the Sulphur level less than 0.01%, Mag-
Coke or magnesium wire is injected into the hot metal.
3. Modifying structure of graphite in cast iron: Mg is effective nodulizer of graphite particles in
cast iron for production of spheroidal graphite (S.G. iron). S.G. iron is stronger, tougher and more
ductile than ordinary cast iron, and is widely used in automotive industry.
4. Pyrotechnics and Photography: Mg emits a brilliant light when ignited. This property is
extensively used in pyrotechnics and photography. Flashlight powder consist of Mg powder mixed
with chemicals which readily give off oxygen when heated, e.g. potassium chlorate, potassium
permanganate and magnesium dioxide.
Uses or Applications of Mg (continue..)
Nonstructural uses (continue..):
5. Cathodic protection: For Pipelines, storage tank bases and lead-sheathed cables, ‘sacrificial’ Mg
anode are placed in the soil and connected by means of insulated wire to the material that is to be
protected against corrosion. In such an arrangement, the corrosion attack is directed preferentially
against the magnesium, and the material is spared.
Structural uses:
Magnesium and aluminum alloys are important for properties like high specific strength, damping
capacity, and resistance to corrosion by chemicals. Consequently, Mg alloys find structural use mainly
in the aircraft industry and also land transportation and material handling.
Extraction of magnesium (mg)

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Extraction of magnesium (mg)

  • 1. Extraction of Mg Department of MME Extraction of Non-Ferrous Metals
  • 2. Details about of Mg Atomic Number: 12 Atomic Weight: 24 amu Density: 1.738 gm/cm 3 Melting Point: 6500 C Boiling Point: 1107 0C
  • 3. Common Minerals of Mg Dolomite – MgCO3.CaCO3 Magnesite – MgCO3 MgCl2 and MgSO4 present in sea water Brucite- [Mg(OH)2] Carnallite- (MgCl2.KCl.6H2O) Olivine- (Mg2SiO4) Serpentine- (Mg3Si2O7) Asbestos – (CaSiO3.3MgSiO3) Kainite- (MgSO4.KCl.3H2O)  Dolomite and magnesite are commercial minerals.  Magnesium hydroxide derived from sea water have sufficiently high Mg content sand do not require upgradation before subsequent extraction.
  • 4. Problems encountered during the extraction of Mg by Pyrometallurgical process MgO is very stable oxide and requires T>1800℃ for carbothermic reduction. Such high temp. is not practicable with external heating. Reduction temp. can be reduce by using vacuum to distil off the Mg and to drive the reduction reaction in forward direction. 𝑀𝑔𝑂 𝑐 + 𝐶 𝑐 ↔ 𝑀𝑔 𝑔 + 𝐶𝑂(𝑔) However, it is very difficult to prevent the backward reaction, and hence carbothermic reduction has not commercially accepted. Reduction of MgO by other reductants like CaC2 and Al at 1200℃ under vacuum is feasible, but not commercially attractive. 𝑀𝑔𝑂 𝑐 + 𝐶𝑎𝐶2 𝑐 → 𝐶𝑎𝑂 𝑐 + 𝑀𝑔 𝑔 + 2𝐶 3𝑀𝑔𝑂 𝑐 + 2𝐴𝑙 𝑙 → 𝐴𝑙2 𝑂3 𝑐 + 3𝑀𝑔 (𝑔)
  • 5. Problems encountered in Electrometallurgy viz. direct electrolysis from aqueous medium Mg requires 2.3V more than H2 for deposition and the hydrogen overvoltage is not sufficiently high to overcome this voltage hydrogen is evolved before magnesium can be deposited. To generate sufficiently high hydrogen overvoltage, amalgam cathode can be employed. It can serve two (2) purposes: 1. Because of its extremely smooth surface, hydrogen overvoltage is rendered difficult. 2. The low activity of Mg in amalgam cathode lowers the Mg deposition potential. However, amalgam cathode has not found commercially acceptable.
  • 6. Extraction of Mg by Pyrometallurgical process
  • 7. PIDGEON Process Thermodynamically pure Si can not reduce MgO when both reactant and products are in their standard state. Therefore, the Pidgeon process reduces pressure to remove the Mg vapor and drive the reduction process. In this process, calsined dolomite is briquetted with powered ferrosilicon (75% Si), and the reduction is carried out under vacuum of 0.1 mm Hg at 1100-1200℃ in an externally heated retort. 𝟐𝑴𝒈𝑶. 𝑪𝒂𝑶 𝒄 + 𝑭𝒆𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝟐𝑪𝒂𝑶. 𝑺𝒊𝑶 𝟐 𝒄 + 𝑭𝒆 (𝒄) ………. (1) Since Mg is the only, it can be easily removed from the reaction chamber to avoid possibility of backward reaction. Presence of CaO lowers the free energy of the reduction reaction. The free energies of the reactions at 1200℃: 𝟐𝑴𝒈𝑶 + 𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝑺𝒊𝑶 𝟐 𝒄 ∆𝑮 𝟎 = 𝟓𝟐 𝒌𝒄𝒂𝒍, ∆𝑯 𝟎 = 𝟏𝟑𝟔 𝒌𝒄𝒂𝒍 …….. (2) 𝟐𝑴𝒈𝑶 + 𝟐𝑪𝒂𝑶 𝒄 + 𝑺𝒊 𝒄 → 𝟐𝑴𝒈 𝒈 + 𝟐𝑪𝒂𝑶. 𝑺𝒊𝑶 𝟐 𝒄 𝑮 𝟎 = 𝟏𝟗 𝒌𝒄𝒂𝒍, ∆𝑯 𝟎 = 𝟏𝟏𝟐 𝒌𝒄𝒂𝒍…(3) At 1200℃ the equilibrium pressure of Mg for reaction (3) is 15 mm Hg, and to attain 1 atm. of Mg about 1700℃ is required. Such high temp. is not practicable with external heating, therefore, Pidgeon process incorporates vacuum to drive the reaction (3) in forward direction. Reaction (6) is highly endothermic. Addition of CaF2 and MgF2 acts as catalyst and speeds up the evolution of Mg vapor.
  • 9. PIDGEON Process (continue..) Reaction Mechanism: The reaction occurs through transient liquid phase at some intermediate stages. Distinct stages of Pidgeon process are: (1) The initial reaction between CaO and Fe-Si produce liquid Ca-Si-Fe alloy, which permeates the briquette and forms a metallic network. The reaction occur at around1000℃ and mildly exothermic. The ternary alloy serves as the main reducing agent. (2) Mg vapors produce by reduction of MgO by Ca-Si-Fe alloy. At this stage, pressure increases rapidly and slows down the rate of reaction. Te subsequent reaction rate is governed by the rate at which Mg can escape from the briquettes. Kinetics of the reaction controlled by the presence of SiO vapor in Pidgeon process as: 𝑀𝑔𝑂 (c) +𝑆𝑖 (c) →𝑀𝑔 (g) +𝑆𝑖𝑂 (g) 2𝑆𝑖𝑂 (g)+2𝐶𝑎𝑂 (c) →2𝐶𝑎𝑂.𝑆𝑖𝑂2 (c) +𝑆𝑖 (c)
  • 10. MAGNETOTHERM Process It is essentially a ferrosilicon reduction process carried out at 1500℃ and the bath is maintained in molten state by the addition of aluminum to form a molten slag.
  • 11. DOW Process: Extraction of Mg from Sea-Water
  • 13. DOW Process: Flow Chart Explanation Developed by the Dow Chemical Company (U.S.A). It involves the collection of Mg as insoluble hydroxide by precipitation with lime as: 𝑀𝑔𝐶𝑙2 + 𝐶𝑎(𝑂𝐻)2→ 𝑀𝑔(𝑂𝐻)2+𝐶𝑎𝐶𝑙2 𝑀𝑔𝑆𝑂4 + 𝐶𝑎(𝑂𝐻)2= 𝑀𝑔(𝑂𝐻)2= 𝐶𝑎𝑆𝑂4 The suspension is distributed to thickeners, in which the hydroxide settle and the cleaner overflow pumped back to the sea. The milk of magnesia (slurry) underflow is pumped to filter tank, and subsequently agitated with 10% HCl, which converts it to a weak solution of chloride. This dilute solution is concentrated and filtered to recover the crystallized solids. The filtrate is then subjected to evaporation to recover remaining chloride. Evaporation is carefully controlled as the hydrous chloride is liable to lose hydrogen chloride, which results in oxide contamination in the final product. The reaction is: 𝑀𝑔𝐶𝑙2. 6𝐻2 𝑂 = 𝑀𝑔𝑂 + 2𝐻𝐶𝑙 + 5𝐻2 𝑂
  • 14. DOW Process: Flow Chart Explanation Electrolysis of Magnesium Chloride: Principle: Mg is reactive metal, has a high decomposition potential. Therefore, during aqueous electrolysis hydrogen evolution occurs before the decomposition of MgCl2Not feasible For electrolysis of MgCl2, the electrolyte is normally composed of 25-30% MgCl2, 15% CaCl2 and 50-60% NaCl. A large amount of flux is necessary to maintain fluidity and to increase the density of the bath so that the liberated metal at cathode floats on the surface of the electrolyte. The theoretical decomposition voltage of dissolved MgCl2 is 3.3, but the resistance of the bath raises the voltage to 6.6. A current of 30,000-50,000 A is employed and the temperature of the electrolytic cell is maintained at 670-730℃. Cell design: The electrolytic cell for Mg extraction may be divided into two (2) categories: lined and unlined. Unlined cell must be provided with separate cathodes, usually made of steel, whereas in case of unlined cell, the steel wall of the cell itself may be used as cathode. Graphite anode is used for both cell. The anodes are inert, therefore, not consumed. The cell operate in an inert atmosphere.
  • 15. DOW Process: Flow Chart Explanation It is necessary to prevent chlorination of metallic product by gaseous choline evolved at the anode. Thus, the metal must be diverted away from the anode zone and recombination prevented by special design features. Cl gas is collected in a special hood and the collection of the metal is facilitated by diverting to a pool. The chlorine set free at the anode is used to dry the incoming MgCl2 and also to chlorinate Mg(OH)2. However, complete drying is both expensive and difficult. Therefore, for electrolyzing a chloride that has been one and two moles of combined water have been evolved.
  • 16. Uses or Applications of Mg Magnesium Non-structural Uses Alloying De-oxidation and De-sulphurization Modifying structure of graphite in cast iron Pyrotechnics and Photography Cathodic protection structural Uses
  • 17. Uses or Applications of Mg Nonstructural uses: 1. Alloying: Mg is widely used in alloying, especially in Al-Based alloys, to improve strength, hardness and corrosion resistance. It also improves mechanical properties of Pb-based alloys containing Ca, Sn and In. 2. Deoxidation and desulphurization: Mg has strong affinity for oxygen, effectively deoxidizes many molten metals. For production of iron and steel, the S content in the BF coke is rather high, and the pig iron contains a large quantity of S. To reduce the Sulphur level less than 0.01%, Mag- Coke or magnesium wire is injected into the hot metal. 3. Modifying structure of graphite in cast iron: Mg is effective nodulizer of graphite particles in cast iron for production of spheroidal graphite (S.G. iron). S.G. iron is stronger, tougher and more ductile than ordinary cast iron, and is widely used in automotive industry. 4. Pyrotechnics and Photography: Mg emits a brilliant light when ignited. This property is extensively used in pyrotechnics and photography. Flashlight powder consist of Mg powder mixed with chemicals which readily give off oxygen when heated, e.g. potassium chlorate, potassium permanganate and magnesium dioxide.
  • 18. Uses or Applications of Mg (continue..) Nonstructural uses (continue..): 5. Cathodic protection: For Pipelines, storage tank bases and lead-sheathed cables, ‘sacrificial’ Mg anode are placed in the soil and connected by means of insulated wire to the material that is to be protected against corrosion. In such an arrangement, the corrosion attack is directed preferentially against the magnesium, and the material is spared. Structural uses: Magnesium and aluminum alloys are important for properties like high specific strength, damping capacity, and resistance to corrosion by chemicals. Consequently, Mg alloys find structural use mainly in the aircraft industry and also land transportation and material handling.