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Thixoforming : Semi-solid Metal Processing

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4.8<br />

Recycling of Aluminium–Lithium Alloys from <strong>Thixoforming</strong> Processes<br />

4.8.1<br />

State of the Art<br />

Since the commercial introduction of Al–Li moulding alloys in the late 1980s, the<br />

question of recycling has presented a challenge in many respects [42]:<br />

. The lithium contained in Al–Li residues represents a value far in excess of the<br />

aluminium content.<br />

. The residues can cause problems if they enter the usual recycling route, especially<br />

in the foil sector.<br />

. To date, the specifications for secondary casting alloys do not indicate any lithium<br />

content and an agglomeration of Al–Li residues is not without consequences,<br />

because in moist conditions it can react with the hydrogen being released.<br />

In order to secure a wider use of this group of alloys, a complete recycling<br />

concept must be developed for the residues that would facilitate 100% reuse of the<br />

recycled Al–Li residues. For recycling, first as far as possible a closed system<br />

( closed-loop recycling ) is desirable, in which the residues can be returned directly<br />

to the existing process and need not be diverted through the entire secondary cycle<br />

for aluminium. In the case of scrap recycling this would probably not be feasible:<br />

because of the problems involved in sorting of separated types of scrap, the lithium<br />

would be lost.<br />

In principle, there are two possibilities for recycling of the thixo-materials. The first<br />

and by far the most sustainable solution would be to retain the valuable alloying<br />

elements within the alloy. This is primarily of interest in the case of clean scrap<br />

materials that could be melted down in molten salt. The second alternative would be<br />

to transfer the alloying elements (Mg, Li) into molten salt in order to reclaim them<br />

subsequently from there if required. Such a procedure could be applied for both clean<br />

and low-quality scrap materials. From the point of view of economy, the same<br />

molten salt should be used that is used in the secondary aluminium industry (70%<br />

NaCl þ 30% KCl with 2–3% CaF 2 additive), in contrast to the very hygroscopic<br />

mixture of LiCl and KCl that has been proposed [43, 44]. Then recycling of the salt slag<br />

produced could be performed in a largely conventional manner.<br />

4.8.2<br />

Thermochemical <strong>Metal</strong>–Salt Equilibria<br />

4.8 Recycling of Aluminium–Lithium Alloys from <strong>Thixoforming</strong> Processesj139<br />

In order to decide which salt mixture compositions come into consideration for<br />

the two above-mentioned recycling alternatives, thermochemical calculations were<br />

performed in respect of the equilibria between the relevant alloys and various molten<br />

salts, using the FACTSAGE program. Four alloy types were combined with salt<br />

mixtures, on the one hand based on NaCl and KCl with added CaF2,MgCl2, LiF and<br />

on the other based on KCl and LiCl.

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