Method of cooling molten metal during fractional crystallisation

Information

  • Patent Grant
  • 7537639
  • Patent Number
    7,537,639
  • Date Filed
    Wednesday, November 10, 2004
    20 years ago
  • Date Issued
    Tuesday, May 26, 2009
    15 years ago
Abstract
Method of cooling an at most partially solidified molten metal during fractional crystallization wherein metal crystals formed have a purer composition than that of the molten metal. Salt in solid form is used to cool the at most partially solidified molten metal.
Description

This application is a § 371 National Stage Application of International Application No. PCT/EP2004/012836,filed on Nov. 10, 2004, claiming the priority of European Patent Application No. 03078689.0 filed on Nov. 19, 2003.


The invention relates to a method of cooling an at most partially solidified molten metal during fractional crystallisation.


Crystallisation methods and apparatus can be used to refine a metal (here used as an abbreviation for metal alloy) in which too high a concentration of a foreign element is present. This foreign element can be present because in the metal made from metal ore, the primary metal, too much of the foreign element is present, or because already used metal is recycled and the foreign element concentration in the scrap is too high. For example aluminium scrap can contain too much of the foreign elements Fe, Si or Mg for use for commercial purposes unless it is mixed with primary metal containing little of the foreign element(s).


During fractional crystallisation metal crystals are formed in the molten metal due to the cooling of the molten metal. The crystals have a composition that is purer than the composition of the molten metal that is used as a starting point or in other words the crystals contain less of the foreign element(s) per unit weight compared to the molten metal that is used as a starting point.


Conventional methods of cooling an at most partially solidified molten metal during fractional crystallisation involve cooling the walls of the crystallisation apparatus by, for example, embedding cooling pipes in the wall. These conventional methods however have the disadvantage that crystals grow on and encrust the cool surfaces. Cooling through the walls of the apparatus, can be supplemented by way of a cooling device using a cooling coil or such an arrangement which is inserted into the molten metal, however such a device will only cool the molten metal at one place and again the molten metal will crystallise on and around the device, hampering the cooling effect of the cooling device.


It is an object of the invention to provide an improved method of cooling an at most partially solidified molten metal during fractional crystallisation, particularly suitable for refinement of aluminium and suchlike metals having a high melting point.


It is another object of the invention to provide a method of cooling an at most partially solidified molten metal during fractional crystallisation with which the solid fraction and/or temperature of the at most partially solidified molten metal can be better controlled compared to the prior art.


It is still another object of the invention to provide a method of cooling an at most partially solidified molten metal during fractional crystallisation which improves the likelihood of the metal crystals remaining in suspension in the molten metal by for example reducing the risk of the metal crystals adhering to the walls of the vessel in which it is contained.


One or more of these objects are achieved by a method of cooling an at most partially solidified molten metal during fractional crystallisation wherein metal crystals formed have a purer composition than that of the molten metal characterised in that salt in solid form is used to cool the at most partially solidified molten metal.


The use of a solid salt to cool the molten metal is advantageous for a number of reasons. When using the method of the present invention the solid salt added absorbs a lot of energy from the molten metal as it warms up from the temperature at which it was added, e.g. approx 20° C., to the temperature of the at most partially solidified molten metal, but crystals are unlikely to form and attach themselves to the molten salt or solid salt particles which means that metal crystals formed remain in suspension in the molten metal. The method of the present invention also allows for accurate dosing of the desired amount of solid salt for cooling. Preferably 0.1 to 1 kg of salt is added to the molten metal per kg of refined metal crystals produced, to ensure sufficient cooling. More preferably 0.2 to 0.8 kg of salt is added to the molten metal per kg of refined metal crystals produced or even more preferably 0.3 to 0.6 kg of salt per kg of refined metal crystals produced.


The solid salt preferably melts at least partially during the cooling of the at most partially solidified molten metal as it preferably has a melting point below the melting point of the at most partially solidified molten metal. The solid salt thus absorbs heat from the molten metal as it warms up and as it melts. The molten salt can be chosen to be either heavier or lighter than the molten metal, so the molten metal will float on the heavier molten salt or the lighter molten salt will float on the molten metal, or both if two types of solid salt are used. The temperature of the molten salt can be measured and controlled to control the temperature of the molten metal, whereas when cooling through the walls of a crystallisation apparatus the temperature of the molten metal can be less accurately controlled. The molten salt does not form a surface on which crystals can form and attach themselves.


At least some of the salt is preferably removed, e.g. by tapping off, once it is molten thereby enabling more solid salt to be added and more cooling to occur.


The removed salt is preferably cooled and solidified for re-use. This makes the method cost effective and economical with resources, as the cooling means can be re-used.


The solid salt is preferably added from above and/or to below and/or into the at most partially molten metal. If solid salt is added from above and/or below the at most partially molten metal it may form a molten salt layer above and/or below the at least partially molten metal e.g. the salt may be added from above the at most partially molten metal and may form a molten salt layer below the at least partially molten metal. If solid salt is added from above and/or below the at most partially molten metal it may also cool an already existing molten salt layer thereby cooling the molten metal via the salt/molten metal interface. When solid salt is added into the at most partially molten metal it will directly cool the molten metal and encourage metal crystal formation.


The at most partially solidified molten metal is preferably stirred. By stirring the at most partially solidified molten metal the metal crystals are kept in suspension and the exchange of material between the metal crystals and the molten metal is enhanced.


The solid salt is preferably added to a vortex formed on the surface of the at most partially solidified molten metal by the motion of the stirrer. The solid salt is added into the vortex created by the rotating motion of the stirrer on the surface of the molten metal which draws the solid salt from the surface into the body of the at most partially solidified molten metal. The solid salt is thus added to the surface of the at most partially molten metal but ends up in the body of the at most partially molten metal where it directly cools the molten metal and encourages metal crystal formation.


The solid salt is preferably added through a means for stirring the at most partially solidified molten metal. The solid salt is thereby well distributed through the molten metal, the salt/metal contact surface is relatively large and the salt effectively encourages metal crystal formation by cooling the metal as it heats up and melts.


The solid salt once molten preferably has a lower density than that of the at most partially solidified molten metal so that it forms a layer on top of the at most partially solidified molten metal and can be easily removed e.g. by tapping off and reduces oxidation of the molten metal.


The solid salt preferably comprises alkaline earth metal halides or alkali metal halides or mixtures thereof as such halides are chemically stable and less likely to react with the at most partially solidified molten metal.


The at most partially solidified molten metal is preferably an aluminium alloy. Fractional crystallisation is particularly suited for aluminium. Recycling aluminium is cost effective in view of the production of primary aluminium being very energy intensive and expensive and it is often necessary to reduce the amount of a foreign element or elements in recycled aluminium in order to obtain a required chemical composition.





The present invention will be further explained by way of example with reference to the accompanying schematic FIGS. 1 to 3.



FIG. 1 shows a cross section through a crystallisation apparatus in which the cooling method according to the invention is implemented.



FIG. 2 shows a cross section through a further crystallisation apparatus in which the cooling method according to the invention is implemented.



FIG. 3 shows a cross section through a further crystallisation apparatus in which the cooling method according to the invention is implemented.






FIG. 1 shows a crystallisation apparatus for implementing the method according to the invention. The apparatus comprises a chamber 9 surrounded by walls 3 and floor portion 4. The apparatus may comprise a lid but this is not shown in the figure. The walls 3 and floor portion 4 are preferably heated by embedded heating elements or pipes 5. The apparatus comprises a stirrer or impeller 6. The rotating motion of the stirrer 6 generates a vortex 14 in the at most partially solidified molten metal 8 which extends up to the surface of the molten metal. The solid salt 13 is dropped or strewn onto the surface of the at most partially solidified molten metal 8 and is preferably oriented to fall into the vortex 14 created by the stirrer so the solid salt is drawn into the body of the at most partially solidified molten metal in the chamber of the apparatus. The salt melts as it has been selected to have a melting temperature below the melting temperature of the metal. The solid salt is also preferably selected to be of greater density once molten than the molten metal and thus forms a layer 11 beneath the at most partially solidified molten metal. Salt can be removed from the layer 11 and once removed may be cooled and solidified for re-use.



FIG. 2 shows a crystallisation apparatus 1 for the fractional crystallisation of a molten metal containing one or more foreign elements. The apparatus comprises a chamber 9 surrounded by a lid 2, walls 3 and floor portion 4. The walls 3 and floor portion 4 are preferably heated by embedded heating elements or pipes 5. The apparatus also comprises a stirrer or impeller 6, which is rotated, and a pipe 7. Solid salt 13 in powder or fine-grained form along with inert gas under pressure is supplied to the at most partially solidified molten metal 8 through the pipe 7. The stirring of the at most partially solidified molten metal keeps the crystals in suspension and enhances the exchange of material between the crystals and the molten metal. The salt melts as its melting temperature is below the melting temperature of the at most partially solid molten metal. The salt once molten preferably has a lower density than that of the molten metal so the salt 13 rises through the at most partially solidified molten metal and forms a layer 11 on top of the metal and can be tapped off via outlet 10. Once tapped off the salt is cooled and solidified for re-use.



FIG. 3 shows an alternative crystallisation apparatus for implementing the method according to the invention. The apparatus comprises a chamber 9 surrounded by a lid 2, walls 3 and floor portion 4. The walls 3 and floor portion 4 are preferably heated by embedded heating elements or pipes 5. The apparatus comprises a combined stirrer and supply pipe 12 for the solid salt. The solid salt 13 is supplied in powder or fine-grained form along with inert gas under pressure to the pipe 12. The gas and solid salt pass through a duct in the interior of the pipe 12 and exit into the at most partially solidified molten metal via at least two openings in the pipe. The pipe 12 is rotated to stir the at most partially solidified molten metal whilst the solid salt is being supplied to the at most partially solidified molten metal. The stirring of the at most partially solidified molten metal keeps the crystals in suspension and enhances the exchange of material between the crystals and the molten metal. The salt once molten preferably has a lower density than that of the molten metal so the salt 13 rises through the at most partially solidified molten metal 8 and forms a layer 11 on top of the metal and can be tapped off via outlet 10. Once tapped off the salt is cooled and solidified for re-use.


The at most partially solidified molten metal 8 is preferably aluminium alloy. The solid salt added may have a density once molten greater than or lower than the density of the molten metal. The salt may thus ultimately form a layer above and in contact with the upper surface of the molten metal or may form a layer beneath and in contact with the lower surface of the molten metal. The solid salt added may also have a composition such that some of the salt once molten forms a layer above the molten metal and some forms a layer below the molten metal. The solid salt may be supplied directly onto the upper surface of the at most partially solidified molten metal and/or may be supplied onto and/or into a salt layer in contact with the upper surface of the at most partially solidified molten metal. The solid salt may be supplied below the lower surface of the at most partially solidified molten metal directly to the lower surface and/or into and/or below a salt layer in contact with the lower surface of the at most partially solidified molten metal. The solid salt may be supplied both above and below the at most partially solidified molten metal. The solid salt may be supplied in for example powder, pellet, lump or large blockform. The solid salt may simply be dropped or immersed into the at most partially molten metal. The solid salt may also be supplied enclosed in another material such as for example in a form comprising a solidified coating of the molten metal.


The solid salt preferably has a melting point below the melting point of aluminium metal and more preferably below 500° C. to ensure the salt stays molten even when forming part of a salt layer positioned above or below the at most partially solid molten metal. The solid salt added preferably comprises halide salts such as alkaline earth metal halides or alkali metal halides or mixtures thereof as such salts are chemically stable and are less likely to react with the molten metal. More preferably the solid salt comprises sodium chloride and magnesium chloride that have respective melting points of 720° C. and 780° C. but in combination can have a significantly lower melting point. Even more preferably approx 60% NaCl and approx 40% MgCl2 is used to achieve a combination of a melting point below 500° C. and chemical stability.


Typical values for cooling effectiveness of solid salt for molten aluminium alloy metal at a temperature of 660° C. are:

    • 1 kg solid salt added at a temperature of 20° C.
    • 1 kg×1000 J/kg° C.×(660-20)° C.=640 kJ (heating salt)
    • 1 kg×300 kJ/kg=300 kJ (melting salt)
    • Total energy absorbed=940 kJ
    • latent heat of fusion of aluminium=390 kJ/kg


Thus to produce 1 kg of aluminium crystals from molten aluminium alloy at 660° C. the amount of salt required for cooling is approx 0.4 kg (390/940 kg).


A reasonable production rate from a crystallisation apparatus containing 500 kg of molten aluminium alloy is 100 kg crystals per hour. Thus to obtain a crystal production rate of 100 kg per hour, 40 kg of solid salt should be supplied per hour.


The lid 2 and/or the layer of molten salt 11 formed in the chamber of the crystallisation apparatus may be heated to a temperature above the melting point of aluminium metal to ensure crystals of aluminium metal do not form on for example the stirrer and/or supply pipe 6,7,12.


Alternatively, elements such as the stirrer and/or supply pipe 6,7,12 could be heated to above the melting temperature of aluminium to avoid encrustation with metal crystals.

Claims
  • 1. A method comprising: cooling an at most partially solidified molten metal during fractional crystallisation, wherein metal crystals formed have a purer composition than that of the molten metal, wherein salt in solid form is used to cool the at most partially solidified molten metal.
  • 2. Method according to claim 1, wherein the salt is chosen that melts at least partially during the cooling of the at most partially solidified molten metal.
  • 3. Method according to claim 1, wherein at least some of the salt is removed once the salt is molten.
  • 4. Method according to claim 3, wherein the removed salt is cooled and solidified.
  • 5. Method according to claim 1, wherein the solid salt is added from above and/or to below and/or into the at most partially solidified molten metal.
  • 6. Method according to claim 1, wherein the at most partially solidified molten metal is stirred.
  • 7. Method according to claim 6, wherein the at most partially solidified molten metal is stirred by a stirrer, wherein the solid salt is added to a vortex formed on the surface of the at most partially solidified molten metal by the motion of the stirrer.
  • 8. Method according to claim 6, wherein the at most partially solidified molten metal is stirred by a means for stirring and solid salt is added into the at most partially solidified molten metal through the means for stirring.
  • 9. Method according to claim 6, wherein the solid salt is chosen to have a lower density once molten than that of the at most partially solidified molten metal.
  • 10. Method according to claim 1, wherein the solid salt comprises alkaline earth metal halides or alkali metal halides or mixtures thereof.
  • 11. Method according to claim 1, wherein the metal is aluminium alloy.
  • 12. Method according to claim 3, wherein the removed salt is cooled and solidified and re-used for cooling at most partially solidified molten metal.
Priority Claims (1)
Number Date Country Kind
03078689 Nov 2003 EP regional
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/EP2004/012836 11/10/2004 WO 00 5/3/2007
Publishing Document Publishing Date Country Kind
WO2005/049875 6/2/2005 WO A
US Referenced Citations (49)
Number Name Date Kind
1562090 Hoopes Nov 1925 A
1938101 Hall Dec 1933 A
3211547 Jarrett et al. Oct 1965 A
3296811 Stoller Jan 1967 A
3303019 Jacobs Feb 1967 A
3308666 Anderson et al. Mar 1967 A
3671229 Ferber et al. Jun 1972 A
3839019 Bruno et al. Oct 1974 A
3840219 Sheridan et al. Oct 1974 A
3840364 Flemmings et al. Oct 1974 A
3849119 Bruno et al. Nov 1974 A
4043802 Esdaile et al. Aug 1977 A
4050683 Langhammer Sep 1977 A
4099965 Beguin et al. Jul 1978 A
4133517 Esdaile et al. Jan 1979 A
4222830 Dawless et al. Sep 1980 A
4239606 Dawless et al. Dec 1980 A
4243211 Leroy et al. Jan 1981 A
4273627 Dawless et al. Jun 1981 A
4305763 Quist et al. Dec 1981 A
4379718 Grantham et al. Apr 1983 A
4411747 Dawless et al. Oct 1983 A
4456480 Wintenberger Jun 1984 A
4581062 Boutin Apr 1986 A
4736314 Riese et al. Apr 1988 A
4744823 Raymond-Seraille May 1988 A
4781771 Masumoto et al. Nov 1988 A
5057150 Reeve et al. Oct 1991 A
5160532 Benz et al. Nov 1992 A
5221377 Hunt, Jr. et al. Jun 1993 A
5312498 Anderson May 1994 A
5405427 Eckert Apr 1995 A
5427602 DeYoung et al. Jun 1995 A
5741348 Van Der Donk et al. Apr 1998 A
5968223 Eckert Oct 1999 A
6143070 Bliss et al. Nov 2000 A
6224648 Verdoes et al. May 2001 B1
6290900 Hatano et al. Sep 2001 B1
6355085 Pillin et al. Mar 2002 B1
6909505 Lucas et al. Jun 2005 B2
7419530 De Vries et al. Sep 2008 B2
7442228 DeVries Oct 2008 B2
20010031823 Atchetee et al. Oct 2001 A1
20040261572 De Vries Dec 2004 A1
20050039578 De Vries et al. Feb 2005 A1
20050145071 Cates Jul 2005 A1
20050178239 De Vries et al. Aug 2005 A1
20060162491 De Vries et al. Jul 2006 A1
20070023110 De Vries et al. Feb 2007 A1
Foreign Referenced Citations (33)
Number Date Country
258283 Jul 1988 DE
4325793 Feb 1995 DE
0099948 Feb 1984 EP
0375308 Jun 1990 EP
0587274 Mar 1994 EP
0696646 Feb 1996 EP
0745693 Dec 1996 EP
0829552 Mar 1998 EP
1288319 Mar 2003 EP
1380659 Jan 2004 EP
1594154 Jun 1970 FR
0615590 Jan 1949 GB
885503 Dec 1961 GB
974829 Nov 1964 GB
1352567 May 1974 GB
2154315 Sep 1985 GB
52135797 Nov 1977 JP
55050442 Apr 1980 JP
57152435 Sep 1982 JP
59205424 May 1983 JP
58104132 Jun 1983 JP
59028538 Feb 1984 JP
60234930 Nov 1985 JP
7070666 Mar 1995 JP
2105084 Feb 1998 RU
2112065 May 1998 RU
2112065 May 1998 RU
1589173 Aug 1990 SU
9827240 Jun 1998 WO
02052053 Jul 2002 WO
2004005558 Jan 2004 WO
2004005559 Jan 2004 WO
2005 095658 Oct 2005 WO
Related Publications (1)
Number Date Country
20070272057 A1 Nov 2007 US