EP1328666A1 - Elaboration d'alliages de type aluminium-silicium - Google Patents
Elaboration d'alliages de type aluminium-siliciumInfo
- Publication number
- EP1328666A1 EP1328666A1 EP01974400A EP01974400A EP1328666A1 EP 1328666 A1 EP1328666 A1 EP 1328666A1 EP 01974400 A EP01974400 A EP 01974400A EP 01974400 A EP01974400 A EP 01974400A EP 1328666 A1 EP1328666 A1 EP 1328666A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- silicon
- less
- grains
- alloys
- particles
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/02—Making non-ferrous alloys by melting
- C22C1/026—Alloys based on aluminium
Definitions
- the invention relates to a process for the production of aluminum-silicon alloys, more particularly alloys with more than 7% silicon, by introducing metallurgical silicon into liquid aluminum.
- Silicon is a fairly common addition element in aluminum alloys, in particular Al-Si-Mg alloys (6000 series) and Al-Si alloys (4000 series). In this last category of alloys, used especially for the manufacture of molded parts, the silicon content can be significant, and sometimes exceed the content of the eutectic, which is around 13%. These alloys can contain other addition elements such as magnesium, copper, manganese, zinc or nickel. The production of these alloys is generally carried out in flame ovens or in induction ovens, at temperatures of approximately 700 to 800 ° C. To the aluminum charge is added from the start of the operation a metallurgical silicon charge corresponding to approximately 75 to 90% of the quantity required.
- the silicon is loaded into pieces and its dissolution in the aluminum takes place gradually during the melting of the charge, which in no way constitutes a brake on the productivity of the furnace.
- a sample is taken for analysis and a complementary addition of silicon is carried out for final titration, an operation whose duration, conditioned by the kinetics of dissolution of the silicon in the alloy mainly based on aluminum. , is likely to limit the productivity of the oven in which the operation is carried out.
- this final addition takes place in the form of silicon obtained from ingots, of mass always greater than 10 kg, crushed then crushed to obtain pieces of less than 10 mm, and, after sieving at 1 mm, a product of size range 1-10 mm.
- the difference in density between the solid silicon and the liquid aluminum alloy being produced is very small, so that the silicon introduced tends to float on the surface of the alloy bath.
- the surface exposed to the atmosphere of the furnace is thereby increased, which has the effect of increasing the oxidation of the metal elements in the oven and the formation of dross at the expense of efficiency.
- the object of the invention is a process for the production of alloys of the Al-Si type, in particular of alloys between 7 and 13% of silicon, in a flame oven or in an induction oven, allowing rapid dissolution of the silicon, a reduction in the number of bath mixes and less formation of dross.
- the subject of the invention is a process for the production of Al-Si alloys by introducing into liquid aluminum, at a temperature between 700 and 850 ° C., metallurgical silicon grains with a particle size of less than 10 mm, in which the grains of silicon, when they reach the temperature of liquid aluminum, have the property of fragmenting into smaller grains.
- the metallurgical silicon grains used are prepared by water granulation of the molten silicon.
- the invention is based on the observation made by the applicant of a different behavior, during the development of aluminum-silicon alloys, between the silicon usually used and obtained by casting ingots, crushing and grinding, and the silicon obtained by granulation. at the water.
- the latter under certain conditions of use, makes it possible to reduce both the duration of dissolution of silicon in liquid aluminum, and the losses of metal by oxidation.
- Metallurgical silicon granulated with water is used for the synthesis of halosilanes which are used for the preparation of silicones, as indicated by the patents EP 0610807 (Wacker Chemie) or EP 0673880 (Pechiney Electrométallurgie).
- a process for granulating silicon with water is described, for example, in patent FR 2723325 (Pechiney Electrométallurgie).
- the Applicant has sought to analyze the differences between these two types of silicon grains.
- a first difference concerns the content of fine particles.
- These very fine particles are probably generated during product packaging and observation of the powder under a microscope confirms their existence.
- the evaluation of their relative quantity by mass can be determined by laser granulometry. There are always in the 1-10 mm particle size range of silicon prepared by the dry route, mass fractions of particles of size less than 5 ⁇ m of the order of at least 0.5%.
- the method of preparation of the product can be used to insert in the process a step of rinsing with water which makes it possible to remove the major part of the particles of size less than 5 .mu.m.
- a step of rinsing with water which makes it possible to remove the major part of the particles of size less than 5 .mu.m.
- the levels of particles below respectively 50 ⁇ m and 5 ⁇ m remain practically unchanged after its subsequent rise in the temperature of the liquid metal.
- the granulation with water of the liquid silicon can give products whose granulometry is between 0 and 30 mm, it is necessary to select from the granulated silicon, by sieving for example, a finer granulometric slice, by limiting oneself at the edge less than 10 mm.
- the process according to the invention makes it possible to obtain Al-Si alloys of a quality at least as good as those prepared with crushed and ground silicon.
- the inclusion quality of the alloys is at the same level, the number of inclusions detected in the alloy not varying significantly.
- the hydrogen contents measured on the liquid alloy are of the order of 0.1 to 0.2 cm 3 of hydrogen per 100 g of alloy. When adding silicon, these contents
- ? 0 vary by plus or minus 10% whatever the type of silicon used, which confirms that the granulated silicon does not constitute a significant supply of hydrogen.
- the inclusion quality control of the liquid metal was done by the K-Mold and LIMCA (Liquid Metal Cleanliness Analysis) tests, the purpose of which is to quantify the concentrations of oxide inclusions to through results expressed in units specific to each of these tests.
- the K-Mold test consists of counting the number of inclusions detected on the fracture surface
- test piece 30 of a test piece poured into a mold of defined shape.
- the results are expressed in number of inclusions reduced to the fracture surface of the test piece. This test can detect large inclusions, typically in the 50 ⁇ m - 300 ⁇ m range.
- the LIMCA control implements material related to the Coulter Counter and makes it possible to evaluate the concentration in the metal of solid inclusions of size between 20 ⁇ m and 150 ⁇ m; the results are expressed in number of inclusions per kg of metal.
- the values observed can range from 1000 inclusions per kg for an alloy considered clean to 100,000 inclusions per kg for a very dirty alloy.
- the hydrogen content is checked by means of an ALSCAN device which allows immediate measurement on the liquid alloy. The results are expressed in cm 3 of hydrogen gas, brought under normal conditions of temperature and pressure, per 100 g of alloy.
- This production was ground to a maximum particle size of 10 mm, then sieved to 1 mm to separate the fraction 1-10 mm. To assess the particle size quality of this product, a sample was taken and then washed with water.
- the washing water was then evaporated to collect the entrained fines which were analyzed using a laser granulometer. We were thus able to reconstruct the true particle size analysis of the original product, which was found to contain 0.51% of fines smaller than 5 ⁇ m.
- the second batch of ground silicon prepared in Example 1 was used during a test in the workshop for manufacturing alloy A-S13 for the title of the bath before casting.
- the operation was carried out in a 5-ton flame oven, the temperature of which was regulated with a set point of 750 ° C.
- For the titration 245 kg of product were added, and between the time of this addition and the final pouring, 47 minutes passed. Two bath stirrings were carried out and at the end of the operation 16 kg of slag were recovered.
- the silicon yield calculated according to the rise in the titer following the addition was 93%.
- the quality control of the AS 13 alloy gave the following elements: Inclusion quality evaluated by the LIMCA method: 1100 inclusions / kg. Hydrogen content: 0.20 cm 3 / 100g.
- Example 1 The third batch of ground silicon prepared in Example 1 was used to repeat the experiment of Example 1 by controlling the temperature of the oven at 810 ° C.
- the time required for the dissolution of the silicon additions was 8 to 10 minutes, which made it possible to estimate the gain due to the effect of the temperature rise at around 20%.
- the fourth batch of ground silicon prepared in Example 1 was used during a test in the workshop for manufacturing alloy A-S13 for the title of the bath before casting.
- the operation was carried out in a 5-ton flame oven, the temperature of which was regulated with a set point of 810 ° C.
- 179 kg of product were added, and between the time of this addition and the final pouring, 28 minutes passed.
- Two bath stirrings were carried out and at the end of the operation 12 kg of slag were recovered.
- the silicon yield calculated according to the rise in the titer following the addition was 94%.
- the quality control of the AS 13 alloy gave the following elements: Inclusion quality evaluated by the LIMCA method: 1400 inclusions / kg Hydrogen content: 0.20 cmVlOO g.
- a test for the manufacture of granulated silicon was carried out on the same industrial installation as that which served to prepare the ground silicon of Example 1, without changing either the charge of the silicon furnace or the operating conditions of the bagging treatment for refining.
- the contents of a pocket of molten silicon at 1530 ° C. were poured onto a tank granulation installation with water.
- the product recovered in the granulation pool was rinsed with water spray before being dried and then sieved to 10 mm.
- the fraction greater than 10 mm has been eliminated and used for other applications. No 1 mm sieving was carried out.
- the 0/10 mm granule obtained was subjected to a particle size control under the same conditions as in Example 1.
- the rate of fines of size less than 5 ⁇ m was 0.03%.
- the chemical analysis of the metal gave:
- the metal thus prepared was separated into two identical batches, one of which was used in the test workshop for placing under baths of Al-Si alloys before casting.
- the operations carried out consisted in raising the silicon title of Al-Si alloys to 0, 6, and 12% Si by 1 point. These operations were carried out in a resistance furnace, at 750 ° C, on crucibles of 100 kg of alloy.
- Example 6 The second batch of granulated silicon prepared in Example 5 was used during a test in the workshop for manufacturing alloy A-S13 for the title of the bath before casting. The operation was carried out in a 5-ton flame oven, the temperature of which was regulated with a set point of 810 ° C. For the title, 256 kg of product were added. The addition and mixing of this addition was very rapid; a single bath stirring was carried out and the casting started only 19 minutes after the addition of silicon. At the end of the operation, only 3.5 kg of slag was recovered.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Silicon Compounds (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Powder Metallurgy (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Manufacture Of Alloys Or Alloy Compounds (AREA)
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0012508A FR2814757B1 (fr) | 2000-10-02 | 2000-10-02 | Elaboration d'alliages de type aluminium-silicium |
FR0012508 | 2000-10-02 | ||
PCT/FR2001/002993 WO2002029126A1 (fr) | 2000-10-02 | 2001-09-27 | Elaboration d'alliages de type aluminium-silicium |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1328666A1 true EP1328666A1 (fr) | 2003-07-23 |
EP1328666B1 EP1328666B1 (fr) | 2004-03-24 |
Family
ID=8854876
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP01974400A Expired - Lifetime EP1328666B1 (fr) | 2000-10-02 | 2001-09-27 | Elaboration d'alliages de type aluminium-silicium |
Country Status (17)
Country | Link |
---|---|
US (1) | US6916356B2 (fr) |
EP (1) | EP1328666B1 (fr) |
JP (1) | JP5243682B2 (fr) |
CN (1) | CN1210419C (fr) |
AT (1) | ATE262600T1 (fr) |
AU (2) | AU9392401A (fr) |
BR (1) | BR0114311B1 (fr) |
CA (1) | CA2424827A1 (fr) |
DE (1) | DE60102485T2 (fr) |
ES (1) | ES2217190T3 (fr) |
FR (1) | FR2814757B1 (fr) |
MX (1) | MXPA03002823A (fr) |
NO (1) | NO331463B1 (fr) |
RU (1) | RU2269583C2 (fr) |
TR (1) | TR200401444T4 (fr) |
WO (1) | WO2002029126A1 (fr) |
ZA (1) | ZA200302314B (fr) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090028740A1 (en) * | 2003-04-14 | 2009-01-29 | S'tile | Method for the production of semiconductor granules |
FR2853562B1 (fr) * | 2003-04-14 | 2006-08-11 | Centre Nat Rech Scient | Procede de fabrication de granules semiconducteurs |
US8192648B2 (en) | 2003-04-14 | 2012-06-05 | S'tile | Method for forming a sintered semiconductor material |
US8405183B2 (en) | 2003-04-14 | 2013-03-26 | S'Tile Pole des Eco-Industries | Semiconductor structure |
JP4869061B2 (ja) | 2003-04-14 | 2012-02-01 | セントレ・ナショナル・デ・ラ・レシェルシェ・サイエンティフィーク | 焼結された半導体材料 |
US9493358B2 (en) | 2003-04-14 | 2016-11-15 | Stile | Photovoltaic module including integrated photovoltaic cells |
US9741881B2 (en) | 2003-04-14 | 2017-08-22 | S'tile | Photovoltaic module including integrated photovoltaic cells |
US20070280328A1 (en) * | 2006-05-30 | 2007-12-06 | Howmet Corporation | Melting method using graphite melting vessel |
CN102690964B (zh) * | 2012-06-13 | 2014-06-18 | 山东大学 | 一种过共晶铝硅合金初生硅变质剂及其制备方法 |
EP2929958A4 (fr) * | 2012-12-10 | 2016-07-13 | Showa Denko Kk | Procédé de production de lingot d'alliage d'aluminium contenant du silicium |
WO2014091936A1 (fr) * | 2012-12-10 | 2014-06-19 | 昭和電工株式会社 | Procédé de production de lingot d'alliage d'aluminium contenant du silicium |
RU2570142C1 (ru) * | 2014-11-20 | 2015-12-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Уральский государственный горный университет" | Способ получения литого алюминиево-кремниевого композиционного сплава |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1463933A (en) * | 1975-02-27 | 1977-02-09 | Diamond Shamrock Corp | Alloying constituents for aluminium |
WO1988002409A1 (fr) * | 1986-09-29 | 1988-04-07 | Vsesojuzny Nauchno-Issledovatelsky I Proektny Inst | Procede pour produire un alliage d'alumino-silicium contenant 2-22 pour cent en poids de silicium |
JPH0611891B2 (ja) * | 1989-10-16 | 1994-02-16 | 日本金属化学株式会社 | ケイ素をアルミニウムに添加する方法 |
FR2729131B1 (fr) * | 1995-01-09 | 1997-02-14 | Pechiney Electrometallurgie | Silicium et ferrosilicium metallurgique a basse teneur en oxygene |
JPH0953131A (ja) * | 1995-08-11 | 1997-02-25 | Miyako Nakada | 金属珪素の溶解方法 |
JPH10182125A (ja) * | 1996-12-20 | 1998-07-07 | Kawasaki Steel Corp | 粉状高純度シリコンの製造方法 |
-
2000
- 2000-10-02 FR FR0012508A patent/FR2814757B1/fr not_active Expired - Fee Related
-
2001
- 2001-09-27 DE DE60102485T patent/DE60102485T2/de not_active Expired - Lifetime
- 2001-09-27 EP EP01974400A patent/EP1328666B1/fr not_active Expired - Lifetime
- 2001-09-27 AU AU9392401A patent/AU9392401A/xx active Pending
- 2001-09-27 RU RU2003112624/02A patent/RU2269583C2/ru not_active IP Right Cessation
- 2001-09-27 MX MXPA03002823A patent/MXPA03002823A/es active IP Right Grant
- 2001-09-27 AU AU2001293924A patent/AU2001293924B9/en not_active Ceased
- 2001-09-27 US US10/380,769 patent/US6916356B2/en not_active Expired - Fee Related
- 2001-09-27 ES ES01974400T patent/ES2217190T3/es not_active Expired - Lifetime
- 2001-09-27 CN CN01817824.3A patent/CN1210419C/zh not_active Expired - Fee Related
- 2001-09-27 AT AT01974400T patent/ATE262600T1/de active
- 2001-09-27 BR BRPI0114311-5A patent/BR0114311B1/pt not_active IP Right Cessation
- 2001-09-27 JP JP2002532691A patent/JP5243682B2/ja not_active Expired - Fee Related
- 2001-09-27 ZA ZA200302314A patent/ZA200302314B/en unknown
- 2001-09-27 WO PCT/FR2001/002993 patent/WO2002029126A1/fr active IP Right Grant
- 2001-09-27 CA CA002424827A patent/CA2424827A1/fr not_active Abandoned
- 2001-09-27 TR TR2004/01444T patent/TR200401444T4/xx unknown
-
2003
- 2003-03-31 NO NO20031463A patent/NO331463B1/no not_active IP Right Cessation
Non-Patent Citations (1)
Title |
---|
See references of WO0229126A1 * |
Also Published As
Publication number | Publication date |
---|---|
MXPA03002823A (es) | 2004-09-10 |
WO2002029126A1 (fr) | 2002-04-11 |
AU2001293924B2 (en) | 2006-02-02 |
CA2424827A1 (fr) | 2002-04-11 |
AU9392401A (en) | 2002-04-15 |
AU2001293924B9 (en) | 2006-06-29 |
JP2004510883A (ja) | 2004-04-08 |
TR200401444T4 (tr) | 2004-08-23 |
EP1328666B1 (fr) | 2004-03-24 |
DE60102485T2 (de) | 2005-03-03 |
ES2217190T3 (es) | 2004-11-01 |
US6916356B2 (en) | 2005-07-12 |
NO20031463D0 (no) | 2003-03-31 |
FR2814757B1 (fr) | 2003-07-11 |
RU2269583C2 (ru) | 2006-02-10 |
CN1210419C (zh) | 2005-07-13 |
JP5243682B2 (ja) | 2013-07-24 |
NO20031463L (no) | 2003-05-27 |
ATE262600T1 (de) | 2004-04-15 |
FR2814757A1 (fr) | 2002-04-05 |
BR0114311A (pt) | 2003-10-14 |
NO331463B1 (no) | 2012-01-09 |
US20040035250A1 (en) | 2004-02-26 |
CN1471589A (zh) | 2004-01-28 |
BR0114311B1 (pt) | 2009-01-13 |
DE60102485D1 (de) | 2004-04-29 |
ZA200302314B (en) | 2004-03-25 |
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