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There are many ways in which metals may be produced in powder form,
- -comminution of solid metal
- - precipitation from solution of a salt;
- - thermal decomposition of a chemical compound;
- reduction of a compound, usually the oxide, in the solid state,
- - electrodeposition,
- - and the atomization of molten metal.
Of these the last three account for the bulk of the powders used.
This has been for long the most widely used method for the production of iron powder. Selected ore is crushed, mixed with carbon, and passed through a continuous furnace where reaction takes place leaving a cake of sponge iron which is then further treated by crushing, separation of non-metallic material, and sieving to produce powder.
Since no refining operation is involved, the purity of the powder is dependent on that of the raw materials.The irregular sponge-like particles are soft, and readily compressible, and give compacts of good green strength.
Refractory metals are normally made by hydrogen reduction of oxides, and the same process can be used for copper.
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By choosing suitable conditions - composition and strength of the electrolyte, temperature, current density, etc., many metals can be deposited in a spongy or powdery state.
Extensive further processing - washing, drying, reducing, annealing and crushing may be required.
Copper is the main metal to be produced in this way but chromium and manganese powders are also produced, by electrolysis. In these cases, however, a dense and normally brittle deposit is formed and requires to be crushed to powder.
Electrolytic iron was at one time produced on a substantial scale but it has been largely superseded by powders made by less costly processes. Very high purity and high density are two distinguishing features.
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In this process molten metal is broken up into small droplets and rapidly frozen before the drops come into contact with each other or with a solid surface.
The principal method is to disintegrate a thin stream of molten metal by subjecting it to the impact of high energy jets of gas or liquid.
Air, nitrogen and argon are commonly used gases, and water is the liquid most widely used. |
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A commercial scale plant was set up in Japan to produce iron powder using paraffin as the atomizing liquid the object being to keep the surface oxygen content as low a possible.
The process was technically successful, but the advantages did not justify, in commercial terms, the extra cost involved.
However, interest has not entirely evaporated and work is going on elsewhere. |
| Shapes of gas atomization powders
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By varying the several parameters: design and configurations of the jets, pressure and volume of the atomizing fluid, thickness of the stream of metal etc. - it is possible to control the particle size distribution over a wide range.
The particle shape is determined largely by the rate of solidification and varies from spherical, if a low heat capacity gas is employed, to highly irregular if water is used. In principle the technique is applicable to all metals that can be melted, and is commercially used for the production of iron, copper, including tool steels, alloy steels, brass, bronze and the low-melting-point metals, such as aluminium, tin, lead, zinc, cadmium.
The readily oxidisable metals, for example chromium-bearing alloys, are being atomized on an increasing scale by means of inert gas, specially argon.
| Shapes of water atomization powders |
Water atomization |
In
addition, there are several other processes that are finding increasing
application, an important one being centrifugal atomization in which
droplets of molten metal are discharged from a rotating source.
There are basically two types of centrifugal atomization processes:
- -
in one a cup of molten metal is rotated on a vertical axis at a speed
sufficient to throw off droplets of molten metal, or a stream of metal
is allowed to fall on a rotating disc or cone;
- in
the other a bar of the metal is rotated at high speed and the free
end is progressively melted e.g. by an electron beam or plasma arc.
This
latter process is called the Rotating Electrode Process (REP), and the
bar may be rotated either on a horizontal or on a vertical axis.
A special advantage of these processes is that they can be carried out
in a sealed vessel in a controlled atmosphere - even vacuum - and thus
produce 'clean' powders of highly reactive metals.
With
the REP process the avoidance of contact with refractory is a potent
means of reducing the number of non-metallic inclusions in the powder,
and in components manufactured from the powder.
Atomization
is particularly useful for the production of alloys in powder form,
since the constituents metals are fully alloyed in the molten state.
Thus each powder particle has the same chemical composition.
Additionally
the process is used to produce compositions such as copper-lead, in
which the lead, though soluble in the liquid state, comes out of solution
on solidification. If a casting of such an alloy is made, serious segregation
of the lead results, but if the liquid is atomized, the end product
is copper powder containing a very fine and uniform distribution of
lead inclusions within each powder particle.
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Brittle materials such as inter-metallic compounds, ferro-alloys - ferro-chromium, ferro-silicon, etc. are pulverised mechanically in ball mills, and a process known as the Coldstream Process is finding increasing application for the production of very fine powders such as are required for injection moulding (qv).
In this process, granular material, which may be coarsely atomized powder, is fed in a stream of gas under pressure through a venturi and is cooled and thereby embrittled by the adiabatic expansion of the gas before impinging on a target on which the granules shatters
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Thermal decomposition of a chemical compound is used in some cases, a notable one being nickel carbonyl.
This Carbonyl Process was originally developed as a means of refining nickel, crude metal being caused selectively to react with carbon monoxide under pressure to form the carbonyl which is gaseous at the reaction temperature and which decomposes on raising the temperature and lowering the pressure.
The same process is used for iron, and carbonyl iron powder finds small scale application where its very high purity is useful.
Recently, demand for very fine powders for the injection moulding process has given a considerable impetus to the carbonyl process.
Typically the particle size of carbonyl iron powder is 1 - 5 m, but, as in the case of nickel, it can be tailored to suit particular requirements.
Another case of thermal decomposition is platinum powder of which is made from sponge produced by heating salt - platinum ammonium chloride. In the Sherritt-Gordon process, nickel powder is made by hydrogen reduction of a solution of a nickel salt under pressure.
Chemical precipitation of metal from a solution of a soluble salt is used in other cases - e.g. silver, powder of which is produced by adding a reducing agent to a solution of silver nitrate. This is, of course, the same basic process as is used to produce black and white photographs.
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The
further processing and the final results achieved in the sintered part
are influenced by the characteristics of the powder:
- particle
size,
- and
size distribution,
- particle
shape,
- structure
- and
surface condition.
A
very important parameter is the apparent density (AD) of the powder,
i.e. the mass of a given volume, since this strongly influences the
strength of the compact obtained on pressing. The AD is a function of
particle shape and the degree of porosity of the particles.
The
choice of powder characteristics is normally based on compromise,
since many of the factors are in direct opposition to each other:
An
increase in the irregularity and porous texture of the powder grain,
i.e. decrease in apparent density, increases the reduction in volume
that occurs on pressing and thus the degree of cold-welding, which,
in turn, gives greater green strength to the compact.
This
increase in contacting surfaces also leads to more efficient sintering.
The
same process is used for iron, and carbonyl iron powder finds small
scale application where its very high purity is useful.
Recently
demand for very fine powders for the injection moulding process has
given a considerable impetus to the carbonyl process.
Typically
the particle size of carbonyl iron powder is 1 - 5 m, but, as in the
case of nickel, it can be tailored to suit particular requirements.
Additionally
the greater reduction in volume necessary to give the required green
density may require greater pressure and consequently larger presses
and stronger dies.
The
ease and efficiency of packing the powder in the die depends to a large
extent on a wide particle size distribution.
So
that the voids created between large particles can be progressively
filled with those of smaller size.
Fine
particle sizes tend to leave smaller pores which are easily closed
during sintering.
An
excess of fines, however, reduces flow properties with the results
already detailed above.
The
purity of the powder is critically important. Impurity levels which
can be tolerated depend to a large extent on the nature and state of
combination of the substances concerned.
For
example, the presence of combined carbon in iron tends to harden the
matrix so that increased pressures are required during compaction.
Free
carbon, however, is often an advantage, acting as a lubricant during
the pressing operation.
Most metal powder grains are coated by a thin oxide film, but in general
these do not interfere with the process, since they are ruptured during
the pressing operation to provide clean and active metal surfaces which
are easily cold-welded.
Their
final reduction under the controlled sintering atmosphere is essential
for complete metal bonding and maximum strength.
Stable
oxide films or included oxide particles, such as SiO2 and Al2O3 are
more serious, since these are generally abrasive and lead to increased
tool wear.
Furthermore
they cannot be reduced during subsequent sintering and their presence
may adversely affect the mechanical properties especially impact strength
of the finished part.
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