removal of Sn, As, a Sb

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Production of Pb

-

bluish-white color when freshly cut

11,34g/cm 3 , melting point 327 ° C

(10,69g/cm 3 )

- boiling point 1740 ° C (vaporizes at 550 ° C)

- bad heat and electrical conductor

- very soft, highly malleable

Usage

-

výroba plášťů zemních kabelů

- radiation shields

bullets and shot

lead -acid batteries

- alloys: PbSb, solder - P bSn,an tifriction alloy PbSnSbcompounds: carbonate, oxides

Occurance only in compounds

galena - PbS cerussite - PbCO

3 anglesite – PbSO

4

-

galena is the most important and widely used

- the main impurities: Cu, Zn, Sb, Fe, As, Sn, Ag, Bi a big amount of gangue

Occurance

only in compounds galena - PbS cerussite - PbCO

3 anglesite – PbSO

4

-

selective&collective (PbZn) concentrate: 40-70% Pb

- other source(40%): waste batteries etc.

Production

Pb is produced mainly by pyro. way

- Reduction smelting: 90%

- ISP: 5 %

- Others: 5%

Production of Pb

Roasting:removal of S, conversion of sulphide into oxide

Sintering: coarsening agllomerate

Reduction smelting

Purification of lead bullion

Roasting and sintering

-

Done together on a (Dwight-Lloyd)sintering machine

providing Pb content under

(mixing raw concentrate with returned agglomerate)

- partial removal of Sn and Sb as As

2

O

3 a Sb

2

O

3

2%

Reduction smelting in lead blast furnace

Obtain as much as possible lead bullion

Dissolve as much as possible noble metals in Pb

Move all gangue and Zn into slag

Separate Cu off Pb in form of matte

Reduction smelting in lead blast furnace

1. zone : under 400 ° C, drying and warming of charge .

2.

zone (reduction) : 400-900 ° C, removal of water, decomposition of carbonate & sulfate, reduction of oxides, sulfidization of Cu 3. zone (melting) : above 900 ° C, streaming down liquid Pb to crucible, dissolution of Au, Ag, Cu, As, Sb,

Sn etc. into lead bullion

Reduction smelting in lead blast furnace

-

charge: coke, air, sinter, CaO

Main reactions

PbO + CO = Pb + CO

2

PbO.SiO

2

+ CaO = PbO + CaO.SiO

Reduction smelting in lead blast furnace

Reduction smelting in lead blast furnace continuous taping, the principle of connected vessels

Construction of the furnace

Products of reduction smelting

lead bullion 90-96% Pb, 0,2-2,5% Cu, 0,5-5% Sb, 0,1-0,8%

As, 0,1-1,5% Sn, 0,06-0,5% Ag

slag 25 - 32% SiO

2

, 34 - 40% FeO, 10 - 16% CaO, 5 - 8%

Al

2

O

3

+ MgO, Pb, ZnO ( 30%)

BF gas

CO, CO

2

, SO

2

, vapor, N

2

, dust (3-50 g/m 3 , 40-80% Pb, toxic)

Refining of lead bullion

- removal of dross and Cu- removal of As, Sn, Sb,- removal

(recovery) of noble metals- removal of Bi

Refining of lead bullion removal of dross:

- stirring at 500 ° C

- physical impurities ascending to the surface of lead melt (difference in specific gravity)

- withdrawing as dross

Refining of lead bullion removal of Cu:

limited dissolution of Cu v Pb at low temp., higher affinity of Cu to S than that of Pb

- 1. step: lowering or increasing temperature of the melt just above of melting point of Pb

- 2. step (350 ° C): adding elemental S to form Cu

2

S

(under 0,002%)

Refining of lead bullion removal of Sn, As, a Sb

higher affinity with oxygen, comparing to Pb

- oxidation with air or with sodium nitrate

- oxidation with air:

500 ° C to remove Sn, 700 ° C-800 ° C to remove As, Sb

Refining of lead bullion removal of Sn, As, a Sb

- oxidation with sodium nitrate (Harris’ refining) + fused sodium hydroxide, 500 ° C

+ oxides As, Sb, Sn have acidic character, reaction with oxides of alkli metals to form arsenate, antimonate (V), stannate

Refining of lead bullion removal of Sn, As, a Sb

- oxidation with sodium nitrate (Harris refining) 2NaNO

3

=

Na

2

O +2.5 O

2

+ N

2

SnO

2

2Sb + 2.5 O

2As + 2.5 O

2

= Sb

2

O

5

2

=AsO

5

As

2

O

5

Sn + O

+ 3Na

2

2

=

O =

2Na

3

AsO

4

= Na

2

SnO

3

Sb

2

O

5

+ 3Na

2

O = 2Na

3

SbO

4

SnO

2

+ Na2O

Refining of lead bullion recovery of noble metals (Parkes’ method)

- de-silvering lead by adding metal Zn to form intermetallic

(higher melting point, lower specific gravity) compound

500C, stirring, cooling almost to consolidation, formation of foam containing noble metals (Ag, Au..)

- removal of Zn by vacuum

Refining of lead bullion removal of Bi atd1.) KrollBetterr’s method (under1%Bi)

- adding Pb-Ca (3- 4% Ca) and Mg metal

- slow cooling from 400 ° C to 360 ° C, foam forming atd2.) electrolytic refining (Bi >1%)

electrolyte : PbSiF

6

+ H

2

SiF

6

(fluorosilicate and fluorosilic acid)

- Pb cathodes

- Bi and noble metals report into do anode slugde

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