Process for the continuous purification of metals by fractional crystallization on a rotary drum

The invention relates to a process for fractional crystallization of metals at the surface of a rotary drum. It is characterized in that the distance between the drum (1) and the bottom of the trough (4) containing the metal in the liquid state is regulated and said trough is divided, in the direction of rotation of the drum (3), into an upstream zone (6) and a downstream zone (7) between which the circulation of liquid is restricted, said distance being regulated in such a way as possibly to permit the crystals to be compressed in the upstream zone, and that the crystals are re-melted in the downstream zone, in order to collect the purified metal in the liquid state. The invention is used in the continuous purification of metals such as in particular aluminum.

The present invention concerns a process for the continuous purification of 
metals by fractional crystallization on a rotary drum. 
The man skilled in the art is well aware that, when cooling an alloy which 
has been previously melted in order to put it into the solid state, the 
first crystals which appear are in most cases different in composition 
from the composition of the alloy used. 
Thus, starting from a basic metal containing another element in a 
concentration C.sub.L, it is possible by fractional crystallization to 
separate off a solid in which the concentration in respect of said element 
has become C.sub.S and such that C.sub.S is lower than C.sub.L. That 
phenomenon has been applied to the purification of metals, in particular 
to remove therefrom impurities which are referred to as eutectic when they 
are in hypoeutectic proportions. That phenomenon was the basis for a 
number of processes, some of which have been patented and which are 
primarily distinguished by the procedure for cooling the alloy, effecting 
exchanges between the liquid and solid phases and separating the crystals. 
Each of those processes gives specific advantages which relate inter alia 
either to the production capacity involved or to the degree of 
purification achieved. 
Thus, French Pat. No 1 594 154 describes a process for purifying aluminium, 
in particular in respect of silicon and iron, which comprises the 
following successive phases: 
causing solidification of a volume of liquid metal contained in an 
externally heated crucible by introducing an internally cooled body, 
collecting at the bottom of the crucible the small crystals which formed, 
causing sintering of the small crystals to produce large crystals, and 
separating the large crystals of pure metal from the impure mother liquor, 
either by siphoning off the latter or by sawing up the billet of metal 
collected after solidification of the whole. 
It is true to say that such a process makes it possible to produce a metal 
in a very high state of purity. However, in the course of one operation, 
it is applied to the amount of impure metal initially introduced into the 
crucible, and it is therefore necessary to include stages for discharging 
and recharging the crucible. That limits the amount of time available for 
the purification step in the true sense and thus results in a relatively 
low level of productivity in comparison with that achieved by a continuous 
process. Moreover, as the level of purity of the crystals depends on that 
of the liquid phase, and as the impurities content of the latter 
progressively increases, the level of purity of the crystals falls and 
finally a product of heterogeneous quality is obtained in the course of 
one operation. 
To overcome those disadvantages, other processes have been put forward for 
effecting such fractional crystallization in a continuous mode. Thus for 
example, French Pat. No. 2 285 915 discloses a process characterised by 
"the formation of a column consisting of a paste of metal crystals in a 
liquid metal; said column comprising a relatively cold zone and a 
relatively hot zone and a continuous temperature gradient between said 
zones". That process also includes the supplementary phases "of 
introducing an impure feed metal into the column and continuously taking 
off a portion of the pure liquid metal from the "hot" zone". 
However, it is recognized in French Pat. No. 2 359 210 that such a process 
encountered difficulties in regard to the flow of the liquid through the 
crystals, and it was necessary for the column to incorporate movable 
mechanical devices so as to impart a reciprocating motion to the crystals. 
The fear then is that such devices which are subjected to the rubbing 
effect of the crystals may be a cause of pollution in the metal being 
treated. 
French Pat. No. 2 390 994 also discloses a process for the purification of 
solid materials "by melting followed by a fresh solidification step 
characterised in that a rotary drum is immersed in the melted solid 
material and that the material to be purified, which clings to the surface 
of the drum and which solidifies thereon, upon issuing from the molten 
mass, passes through a zone which is disposed downstream and in which the 
solidified substance clinging to the drum is subjected to re-melting." 
Such a process has been successfully applied to the purification of metals 
such as silicon and germanium. 
However, it is found that the application of that process to other metals 
such as aluminium for example results in the formation of a layer of 
crystals having a certain degree of porosity on the drum, whence the layer 
is impregnated by impure mother liquor and there is a drop in the quality 
of the product obtained. In addition, the adhesion of the crystals to the 
surface of the drum is sometimes very great, which makes it difficult to 
recover them and may result in their being polluted by the material of the 
drum. 
In addition, as those crystals do not have any cohesion with each other, 
they are unsuitable for metallurgical transformation operations and must 
therefore be re-melted beforehand. That is a handicap in comparison with 
processes which result in a metal in the liquid state, which can be cast 
in a solid form which can be used directly. 
Finally, when treating metals which easily undergo oxidation, it is not 
possible to put the crystals which issue in a hot condition from the bath 
directly into contact with the atmosphere without giving rise to a certain 
amount of pollution by the air. It is therefore necessary to provide 
sealed installations which detrimentally affect the cost of the equipment 
required for carrying such a process into effect. 
It is for that reason that the present applicants, being aware of the 
attraction of continuous processes but also being conscious of the 
difficulties inherent in each thereof, sought to find new ways of 
overcoming such disadvantages while also achieving further advantages. The 
applicants' work resulted in the development of a process for the 
continuous purification of metals by fractional crystallization on a 
cooled portion of the surface of a rotary drum partially immersed in a 
bath of molten metal contained in a trough characterised in that the 
distance between the drum and the bottom of the trough is controlled and 
the trough is divided in the direction of rotation of the drum into an 
upstream zone and a downstream zone which are virtually independent of 
each other, that the downstream zone is heated and the crystals are 
completely re-melted within the bath, and that at least a portion of the 
purified liquid resulting from the re-melting operation is taken off in 
said zone. 
Thus, as in the prior art, the process according to the invention involves 
using a drum with a horizontal axis, the diameter thereof generally being 
between 20 and 200 cm and the drum being made of a material which is 
insoluble in the bath of metal to be treated. The drum is driven with a 
rotary movement about its axis at a speed which can be varied by 
mechanical means such as a motor-reducing unit for example. The drum is 
partially immersed in the metal bath which is maintained in the liquid 
state by suitable heating means and contained in a trough which is also of 
insoluble material and the bottom of which is generally parallel to the 
generatrices of the drum. 
The surface of the drum is cooled to a temperature which is lower than the 
solidification temperature of the bath either naturally or by projecting a 
cold-carrier fluid such that, at the time at which it passes into the 
bath, it is covered with a layer of crystals, the thickness of which 
increases as it progresses. 
However, unlike the prior art wherein the layer of crystals grew throughout 
the period for which the surface was immersed and was collected on issuing 
from the bath, the process according to the invention involves 
interrupting that growth and providing for complete re-melting of the 
crystals within the bath. The re-melting operation is carried out by 
passing the drum, at a given time, into a zone of the trough which is at a 
temperature higher than the melting temperature of the crystals and which, 
as considered in the direction of rotation of the drum, is disposed 
downstream of the upstream zone where the crystallization step occurs. 
That zone may be heated by any suitable means. Such means may be for 
example an immersion heater which is immersed in the downstream zone in 
the proximity of the layer of crystals and which uses the energy either of 
a hot fluid or an electrical current. The heating means may also comprise 
heating the portion of the drum, on which the crystal re-melting effect is 
to occur. In order to achieve such a result, use is made of a drum which 
rotates around a fixed hollow shaft. The shaft is provided with two radial 
sectors which extend over the entire length of the drum and which extend 
as far as the wall of the drum against which they slide, and between them 
they form an angle such that on the wall of the drum they define the 
surface portion which is to undergo reheating. A hot fluid is caused to 
circulate in the volume which is thus defined, by means of the hollow 
shaft, or else electrically heated elements are disposed therein. 
Thus, the crystal remelting operation makes it possible to avoid pollution 
of the pure metal by oxidation or by the material of the drum, as occurred 
with the prior art methods. However, it is found to be difficult for such 
a process to be carried out in the arrangements of the prior art for, 
because of the relatively substantial distance between the layer of 
crystals and the bottom of the trough and the entrainment movement 
produced in the bath by the rotary motion of the drum, mixing of the bath 
in the upstream and downstream zones occurs so that the liquid which is 
taken off from the downstream zone is little different in purity from the 
initial liquid introduced into the upstream zone. 
It is in order to prevent mixing of the bath in the two zones that the 
invention is also characterised in that the distance between the drum and 
the bottom of the trough is controlled and the trough is divided into an 
upstream zone and a downstream zone which are virtually independent of 
each other. 
As noted hereinbefore, the layer of crystals which is deposited on the drum 
has a tendency to grow progressively as it passes through the upstream 
zone of the trough and then to decrease in the downstream zone by virtue 
of the remelting operation. Therefore, the layer of crystals locally has a 
maximum thickness, a sort of excrescence, which, by virtue of the symmetry 
of the apparatus, extends along the length of a generatrix of the drum. It 
is along that generatrix that the operation of controlling the distance 
between the drum and the bottom of the trough is preferably effected as 
the presence of that excrescence formed by the crystals may be used to 
limit the movement of liquid from one zone of the trough to the other. 
The distance control operation may simply consist of bringing the surface 
of the drum and the bottom of the trough towards each other so as to give 
a restricted space through which the flow of the liquid is retarded, but 
it is preferable for the layer of crystals, at the location of the local 
excrescence, to come into contact with the bottom of the trough in order 
to prevent the flow of liquid between the zones in question. 
However, under those conditions, it was found that certain crystals formed 
porous accumulations within which a relatively substantial amount of the 
bath collected so that impure metal was transported towards the downstream 
re-melting zone which consequently resulted in a drop in the level of 
purity of the metal. 
It is for that reason that the operation of controlling the distance 
between the drum and the bottom of the trough is also carried out in such 
a way as to adjust that distance between the drum and the bottom of the 
trough, in the region in which the distance is controlled, to a value 
which is less than the thickness of the crystal excrescence. By operating 
in that way, the crystals are compressed and the bath is expelled from the 
mass thereof before they pass into the downstream re-melting zone. Such a 
distance control action has been found to be particularly effective in 
regard to the purity of the metal produced. 
There are two ways of controlling the distance between the drum and the 
bottom of the trough, which comprise either using a trough which has a 
bottom of a particular shape or displacing the drum with respect to the 
trough. 
As regards the bottom of the trough, in the region of the restricted space 
it may be of a circular configuration which is concentric with the surface 
of the drum so as to create a volume which is in the shape of a portion of 
a ring. That volume is extended on respective sides of the drum by two 
upstream and downstream volumes, forming kinds of bath reserve, which are 
provided with means for supplying metal to be purified and for removing 
the purified liquid and the liquid which has become charged with 
impurities in the course of the treatment. 
However, in the situation where the crystals are not subjected to a 
compression effect, the ring portion may serve as a trap for the impure 
bath. It is for that reason that it is preferable for the bottom of the 
trough to be of a configuration such that the space between the drum and 
the bottom of the trough decreases in the upstream zone and increases in 
the downstream zone, as considered in the direction of rotation of the 
drum. The location at which the space is at a minimum approximately 
corresponds to the generatrix of the cylinder on which the crystal 
excrescence is disposed. The above-indicated space may be greater than the 
height of the crystal excrescence but preferably it is the same or, 
better, less, so that the crystals are compressed and the liquid is 
expelled towards the upstream zone. 
The drum-trough bottom distance control may also be achieved by moving the 
drum with respect to the botton of the trough with a cyclic movement 
comprising a translatory movement of the drum in a downward direction, a 
rotary movement over the bottom of the upstream zone of the trough and a 
return to the initial position. 
In its translatory movement downwardly, the drum comes to bear against the 
layer of crystals at the location at which it is of maximum thickness so 
that the crystals are compressed. Then, by rolling over the bottom of the 
trough, the drum compresses the layer of crystals which is disposed 
upstream, while urging the liquid towards the upstream reserve of the 
trough. The liquid displacement movement may affect all or part of the 
surface portion of the drum which is covered with crystals. Finally, the 
drum is returned to its initial position and the normal rotary movement of 
the drum which had been interrupted just before the cycle took place is 
then resumed. 
Such a cyclic movement may be produced by any mechanical means which are 
known to the man skilled in the art and which operate on the position of 
the axis of the cylinder and on its rotary movement. 
That form of control is applied to a trough that is of a shape which is 
concentric with the drum but it may be combined with the trough of special 
shape. 
The cyclic movement occurs with a certain periodicity which is linked to 
the rotary movement of the drum. Thus, it is initiated after a period of 
rotary movement which is at most equal to the time required for a point on 
the drum to pass through the whole of the upstream zone. In that way, it 
is considered that all the layer of crystals is subjected to the 
compression treatment and there is no danger of impure liquid being 
entrained therewith into the downstream zone. 
The process according to the invention may be improved by making the trough 
of a shape such that the volume of the downstream zone is greater than the 
volume of the upstream zon. That makes it possible to have a more 
substantial reserve supply of hot liquid and to facilitate the re-melting 
operation, thus ensuring that a part of the crystals does not emerge from 
the bath. 
When a very high level of metal purity is to be obtained, the process may 
be carried out in apparatuses which are disposed in a series of "n" 
stages. For example, in a two-stage system, the purified liquid issuing 
from the first stage supplies the second stage while the impure mother 
liquid from the second stage is recycled to the feed for the first stage. 
The amounts of liquid which circulate in each of the apparatuses 
corresponds at all times to the following equation: the amount of liquid 
introduced into the upstream zone is equal to the amounts of liquid which 
are drawn off in the upstream and downstream zones. The process according 
to the invention uses a drum, the speed of rotation of which is controlled 
to give a produce of the desired level of purity. In accordance with the 
prior art, that speed is so determined that the residence time of the 
surface of the drum which is immersed in the bath is equal to a certain 
value corresponding to the diameter of the drum multiplied by a certain 
coefficient. That coefficient essentially depends on the nature of the 
metal to be deposited, and the temperatures of the bath and the drum, 
being parameters which may vary in the course of the operation and 
generally result in random levels of purity.

Referring to FIG. 1, shown therein is the drum 1 which is driven with a 
rotary movement about its aixs 2 as indicated by the arrow 3, being 
partially immersed in a trough or channel 4 and cooled naturally and, with 
said trough, forming a restricted space 5 in the shape of a portion of a 
ring, which divides it into two upstream and downstream zones 6 and 7 
respectively, which form reserves of metal whose impurities content is 
increasing and purified metal respectively. The crystals 8 form on the 
immersed portion of the cylinder a layer which has an excrescence which 
creates a constriction between the two zones. Heating means 9 permit the 
bath in the upstream zone to be maintained in the liquid state while the 
non-immersed portion of the drum is cooled by cold fluid distributing 
assemblies 10. Re-melting of the crystals is effected by reheating the 
surface portion of the drum which is between the two sectors 11 by means 
of a hot fluid supplied by way of the hollow shaft 2 and intake and outlet 
openings provided in the tube. The arrows 13, 14 and 15 respectively 
indicate the point at which metal to be purified is introduced, the point 
at which pure liquid is drawn off and the point at which mother liquid 
charged with impurities is drawn off. FIG. 2 shows a trough 4 of a 
particular shape in which the space between the drum 1 and the bottom of 
the trough progressively decreases in the upstream zone 16 and 
progressively increases in the downstream zone 17 and wherein the crystal 
excrescence corresponds to the minimum space between the drum and the 
trough. 
FIGS. 3 to 6 show the different sequences in the cyclic movement of the 
drum. In FIG. 3, the drum is in a condition of normal rotation. In FIG. 4, 
it is undergoing a vertical translatory movement as indicated at 18. In 
FIG. 5, the drum is rolling on the bottom of the downstream zone of the 
trough so as to compress the crystals over a length of the trough 
corresponding to the arc 19. In FIG. 6, the drum has returned to its 
initial position. 
FIG. 7 is a plan view of the drum 1 which rotates in the direction 
indicated by the arrow 3, and the upstream and downstream zones 6 and 7 of 
the trough. The metal to be purified is supplied at 13 while the purified 
liquid is drawn off at 14 and the liquid which has been enriched with 
impurities is taken off at 15. 
FIG. 8 shows a two-stage purification system, that is to say, a system 
comprising two drums 1 and 1' which respectively rotate in the directions 
indicated by the arrows 3 and 3', being partially immersed in the troughs 
4 and 4' and forming the upstream zones 6, 6' and the downstream zones 7, 
7'. The metal to be purified is introduced at 13 into the upstream zone 6, 
crystallized on the drum 1, and re-melted in the downstream zone 7, and 
the liquid is introduced at 14 into the upstream zone 6' where it is 
crystallized on the drum 1' and then re-melted in the downstream zone 7' 
where it is recovered in a highly pure state at 14'. The impurity-charged 
liquid which is taken off at 15' in the upstream zone 6' is recycled to 
the feed at 13 while the very impure liquid formed in the downsteam zone 6 
is taken from the circuit at 15. 
The invention may be illustrated by reference to the following example of 
use wherein an aluminium alloy containing 0.2% by weight of iron was 
treated in accordance with the process in the apparatus shown in FIG. 7 
wherein the drum was 0.5 meter in diameter and rotated at a speed of one 
revolution per minute. For a temperature of the wall of the drum of 
600.degree. C., at the time at which it passed into the bath, a 
temperature of the metal of 670.degree. C. in the upstream zone and 
temperature differences of 50.degree. C. between the downstream and the 
upstream zones and 10.degree. C. between the point at which the 
impurities-charged liquid was taken off and the point of supply with metal 
to be purified, the system produces a purified aluminium which contained 
not more than 0.05% of iron and a mother liquid having an iron content of 
1%. 
The invention can be used in all treatments for the continuous purification 
of metals and in particular aluminium.