BE496600A - - Google Patents
Info
- Publication number
- BE496600A BE496600A BE496600DA BE496600A BE 496600 A BE496600 A BE 496600A BE 496600D A BE496600D A BE 496600DA BE 496600 A BE496600 A BE 496600A
- Authority
- BE
- Belgium
- Prior art keywords
- sep
- hexachlorcyclohexane
- metal
- metals
- degassing
- Prior art date
Links
- 229910052751 metal Inorganic materials 0.000 claims description 22
- 239000002184 metal Substances 0.000 claims description 22
- JLYXXMFPNIAWKQ-UHFFFAOYSA-N γ Benzene hexachloride Chemical compound ClC1C(Cl)C(Cl)C(Cl)C(Cl)C1Cl JLYXXMFPNIAWKQ-UHFFFAOYSA-N 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 9
- 238000007872 degassing Methods 0.000 claims description 7
- 150000002739 metals Chemical class 0.000 claims description 7
- 229910001234 light alloy Inorganic materials 0.000 claims description 5
- 238000007670 refining Methods 0.000 claims description 5
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- SYSQUGFVNFXIIT-UHFFFAOYSA-N n-[4-(1,3-benzoxazol-2-yl)phenyl]-4-nitrobenzenesulfonamide Chemical class C1=CC([N+](=O)[O-])=CC=C1S(=O)(=O)NC1=CC=C(C=2OC3=CC=CC=C3N=2)C=C1 SYSQUGFVNFXIIT-UHFFFAOYSA-N 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- DCXXMTOCNZCJGO-UHFFFAOYSA-N Glycerol trioctadecanoate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 238000009864 tensile test Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 description 1
- WPPDFTBPZNZZRP-UHFFFAOYSA-N aluminum copper Chemical compound [Al].[Cu] WPPDFTBPZNZZRP-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001639 boron compounds Chemical class 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- VHHHONWQHHHLTI-UHFFFAOYSA-N hexachloroethane Chemical compound ClC(Cl)(Cl)C(Cl)(Cl)Cl VHHHONWQHHHLTI-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- -1 melting point Chemical class 0.000 description 1
- UNFUYWDGSFDHCW-UHFFFAOYSA-N monochlorocyclohexane Chemical compound ClC1CCCCC1 UNFUYWDGSFDHCW-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/06—Obtaining aluminium refining
- C22B21/064—Obtaining aluminium refining using inert or reactive gases
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
<Desc/Clms Page number 1>
PROCEDE DE DEGAZAGE DES METAUX ET ALLIAGES LEGERS.
La présente invention concerne un procédé perfectionné de dégazage des métaux et alliages légers de fonderie.
On sait que ces produits s'altèrent rapidement, au cours de la fu- sion, par dissolution de gaz et formation d'oxydes. Les pièces coulées, obte- nues à partir de métaux fondus non traités, sont poreuses et chargées d'in- clusions.
Pour éviter ces inconvénients, on a proposé de faire barboter du chlore dans le métal fondu avant d'opérer la coulée. Ce procédé de dégazage, bien qu'efficace, est très peu répandu en raison des difficultés inhérentes à la manipulation du chlore. Dans un procédé amélioré, il a été préconisé de remplacer le barbotage de chlore par l'introduction d'hexachloréthane solide qui, à la' température de fusion, libère progressivement du chlore par décom- position thermique,
On a maintenant découvert le fait surprenant que l'hexachlorcyclo- hexane, malgré sa teneur relativement élevée en hydrogène et bien que les produits de sa décomposition thermique ne contiennent que peu ou pas de chlo- re,
peut avantageusement servir de produit actif dans les charges affinantes utilisées pour le dégazage et l'affinage des métaux et alliages légers. l'hexachlorcyclohexane technique est généralement obtenu par chlo- ration additive du benzène. Le produit brut de chloration est constitué d'un mélange d'isomères dans lequel l'isomère @ prédomine. Bien que le mélange de ces isomères convienne pour effectuer le dégazage selon le procédé de la pré- sente invention, on utilise de préférence l'isomère @, un mélange enrichi en isomères 0(' ou tout autre hexachlorcyclohexane sous-produit de la fabrication de l'isomère @.
La composition de dégazage à base d'hexachlorcyclohexane est avan- tageusement utilisée sous forme de briquettes ou pastilles de 40 à 50 grammes.
Cette composition peut contenir des substances d'appoint tels que carbonate de soude et stéarine qui facilitent le briquetage ou le pastillage ainsi que des produits connus ayant des propriétés affinantes du grain du métal. De bons résultats ont été obtenus avec-descompositions contenant au moins 50% d'hexa-
<Desc/Clms Page number 2>
chlorcyclohexane, le restant étant constitué d'un mélange d'halogénures à bas point, de fusion, de composés du bore, carbonate de soude, stéarine, etc.
La quantité d'hexachlorcyclohexane à mettre en oeuvre varie avec la nature et les impuretés du métal. Généralement 1 gr d'hexachlorcyclohexane par kilogramme de métal fondu donne des résultats très satisfaisants. Une amélioration sensible peut déjà être observée lorsqu'on ajoute 0,25 gr d' hexachlorcyclohexane par kilogramme de métal.
EXEMPLE I.-
Un alliage du type ALPAX (aluminium-silicium) est traité par de l'hexachlorcyclohexane @ à raison de 1 gr/Kgr de métal.
L'examen microphotographique d'échantillon prélevés dans le métal coulé montre que les porosités se trouvant dans le métal non traité sont tota- lement absentes du métal traité à l'hexachlorcyclohexane. La structure du grain du métal traité est aussi nettement plus fine. Ces observations sont confirmées par les essais de traction qui indiquent une charge de rupture de 12,4 Kgr/mm2 pour l'échantillon prélevé dans le métal traité par l'hexachlorcylclohexane a- lors qu'elle n'est que de 9,2 Kgr/mm2 pour l'échantillon de métal non traité.
Les allongements sont respectivement de 6,3 et 3,2%.
EXEMPLE II .-
Un alliage aluminium-cuivre, à faible teneur en cuivre, est traité après fusion par une composition affinante ayant la composition suivante :
EMI2.1
<tb> Hexachlorcyclohexane <SEP> @ <SEP> 600
<tb>
<tb>
<tb> Chloruré <SEP> de <SEP> sodium <SEP> 75
<tb>
<tb>
<tb>
<tb> Chlorure <SEP> de <SEP> potassium <SEP> 75
<tb>
<tb>
<tb>
<tb> Nitrate <SEP> de <SEP> potassium <SEP> 40
<tb>
<tb>
<tb>
<tb> Fluorure <SEP> de <SEP> sodium <SEP> 15
<tb>
<tb>
<tb>
<tb> Fluosilicate <SEP> de <SEP> sodium <SEP> 15
<tb>
<tb>
<tb>
<tb> Acide <SEP> borique <SEP> 100
<tb>
<tb>
<tb>
<tb> Carbonate <SEP> de <SEP> soude <SEP> 50
<tb>
<tb>
<tb>
<tb> Stéarine <SEP> 30
<tb>
<tb>
<tb>
<tb>
<tb> 1000
<tb>
L'affinant est introduit sous forme de pastilles de 40 gr environ à raison de 1 gr/Kgr de métal.
Les essais de traction indiquent une charge de rupture de 15,6 Kgr/mm2 pour l'échantillon traité et de 14,6 Kgr/mm2 pour l' échantillon non traité. Les allongements sont respectivement de 5,7 et 1,2%.
REVENDICATIONS le- Procédé de dégazage de métaux et alliages légers 'caractérisé en ce que l'on traite le métal fondu par de l'hexachlorcyclohexane.
<Desc / Clms Page number 1>
DEGASING PROCESS FOR METALS AND LIGHT ALLOYS.
The present invention relates to an improved process for degassing foundry metals and light alloys.
It is known that these products deteriorate rapidly, during the fusion, by dissolution of gases and formation of oxides. Castings, obtained from untreated molten metals, are porous and loaded with inclusions.
To avoid these drawbacks, it has been proposed to bubble chlorine in the molten metal before operating the casting. This degassing process, although effective, is not widely used because of the difficulties inherent in handling chlorine. In an improved process, it has been recommended to replace the bubbling of chlorine by the introduction of solid hexachloroethane which, at the melting temperature, gradually releases chlorine by thermal decomposition,
It has now been discovered the surprising fact that hexachlorcyclohexane, despite its relatively high hydrogen content and although the products of its thermal decomposition contain little or no chlorine,
can advantageously serve as an active product in the refining charges used for the degassing and refining of metals and light alloys. technical hexachlorcyclohexane is generally obtained by additive chlorination of benzene. The crude chlorination product consists of a mixture of isomers in which the @ isomer predominates. Although the mixture of these isomers is suitable for carrying out the degassing according to the process of the present invention, the @ -isomer, a mixture enriched in O ('isomers or any other hexachlorcyclohexane by-product of the manufacture of the @ isomer.
The hexachlorcyclohexane-based degassing composition is advantageously used in the form of briquettes or pellets of 40 to 50 grams.
This composition may contain additional substances such as sodium carbonate and stearin which facilitate briquetting or pelletizing as well as known products having properties of refining the grain of the metal. Good results have been obtained with compositions containing at least 50% hexa-
<Desc / Clms Page number 2>
chlorcyclohexane, the remainder being a mixture of low point halides, melting point, boron compounds, sodium carbonate, stearin, etc.
The amount of hexachlorcyclohexane to be used varies with the nature and the impurities of the metal. Generally 1 g of hexachlorcyclohexane per kilogram of molten metal gives very satisfactory results. A significant improvement can already be observed when adding 0.25 g of hexachlorcyclohexane per kilogram of metal.
EXAMPLE I.-
An alloy of the ALPAX type (aluminum-silicon) is treated with hexachlorcyclohexane @ at a rate of 1 gr / kg of metal.
Microphotographic examination of samples taken from the cast metal shows that the porosities found in the untreated metal are completely absent from the metal treated with hexachlorcyclohexane. The grain structure of the treated metal is also significantly finer. These observations are confirmed by the tensile tests which indicate a breaking load of 12.4 Kgr / mm2 for the sample taken from the metal treated with hexachlorcylclohexane a- when it is only 9.2 Kgr / mm2 for the untreated metal sample.
The elongations are 6.3% and 3.2% respectively.
EXAMPLE II .-
An aluminum-copper alloy, with a low copper content, is treated after melting with a refining composition having the following composition:
EMI2.1
<tb> Hexachlorcyclohexane <SEP> @ <SEP> 600
<tb>
<tb>
<tb> Chloride <SEP> of <SEP> sodium <SEP> 75
<tb>
<tb>
<tb>
<tb> <SEP> potassium <SEP> <SEP> 75 chloride
<tb>
<tb>
<tb>
<tb> Nitrate <SEP> of <SEP> potassium <SEP> 40
<tb>
<tb>
<tb>
<tb> <SEP> sodium <SEP> fluoride <SEP> 15
<tb>
<tb>
<tb>
<tb> Fluosilicate <SEP> of <SEP> sodium <SEP> 15
<tb>
<tb>
<tb>
<tb> Boric <SEP> <SEP> 100
<tb>
<tb>
<tb>
<tb> Carbonate <SEP> of <SEP> soda <SEP> 50
<tb>
<tb>
<tb>
<tb> Stearin <SEP> 30
<tb>
<tb>
<tb>
<tb>
<tb> 1000
<tb>
The refiner is introduced in the form of tablets of approximately 40 g at a rate of 1 g / kg of metal.
The tensile tests indicate a breaking load of 15.6 Kgr / mm2 for the treated sample and 14.6 Kgr / mm2 for the untreated sample. The elongations are 5.7 and 1.2% respectively.
CLAIMS the process for degassing metals and light alloys' characterized in that the molten metal is treated with hexachlorcyclohexane.
Claims (1)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE496600A true BE496600A (en) |
Family
ID=139778
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE496600D BE496600A (en) |
Country Status (1)
| Country | Link |
|---|---|
| BE (1) | BE496600A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2512836A1 (en) * | 1981-09-14 | 1983-03-18 | Spolek | PROCESS FOR PREPARING SOLID REFINING AGENTS FOR REFINING ALUMINUM AND ITS ALLOYS |
-
0
- BE BE496600D patent/BE496600A/fr unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2512836A1 (en) * | 1981-09-14 | 1983-03-18 | Spolek | PROCESS FOR PREPARING SOLID REFINING AGENTS FOR REFINING ALUMINUM AND ITS ALLOYS |
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