EP0419378B1 - Begasungsvorrichtung für ein stationäres Aluminium-Schmelzbad mit grosser Oberfläche - Google Patents
Begasungsvorrichtung für ein stationäres Aluminium-Schmelzbad mit grosser Oberfläche Download PDFInfo
- Publication number
- EP0419378B1 EP0419378B1 EP90420406A EP90420406A EP0419378B1 EP 0419378 B1 EP0419378 B1 EP 0419378B1 EP 90420406 A EP90420406 A EP 90420406A EP 90420406 A EP90420406 A EP 90420406A EP 0419378 B1 EP0419378 B1 EP 0419378B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- bath
- furnace
- rotor
- gas
- stator
- 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.)
- Expired - Lifetime
Links
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 11
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 239000004411 aluminium Substances 0.000 title claims 2
- 239000007789 gas Substances 0.000 title description 37
- 230000003068 static effect Effects 0.000 title 1
- 230000000712 assembly Effects 0.000 claims abstract description 13
- 238000000429 assembly Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 4
- 238000002347 injection Methods 0.000 claims description 17
- 239000007924 injection Substances 0.000 claims description 17
- 238000002156 mixing Methods 0.000 claims description 5
- 239000006096 absorbing agent Substances 0.000 abstract 1
- 230000035939 shock Effects 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 description 22
- 239000002184 metal Substances 0.000 description 22
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 9
- 239000012535 impurity Substances 0.000 description 8
- 239000000460 chlorine Substances 0.000 description 7
- 229910052801 chlorine Inorganic materials 0.000 description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000013019 agitation Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 229910001338 liquidmetal Inorganic materials 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 3
- 244000309464 bull Species 0.000 description 3
- VHHHONWQHHHLTI-UHFFFAOYSA-N hexachloroethane Chemical compound ClC(Cl)(Cl)C(Cl)(Cl)Cl VHHHONWQHHHLTI-UHFFFAOYSA-N 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910000952 Be alloy Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000940835 Pales Species 0.000 description 1
- 206010033546 Pallor Diseases 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000002238 attenuated effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000701 toxic element Toxicity 0.000 description 1
- 230000017105 transposition Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D27/00—Stirring devices for molten material
-
- 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
-
- 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
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/05—Refining by treating with gases, e.g. gas flushing also refining by means of a material generating gas in situ
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/16—Introducing a fluid jet or current into the charge
Definitions
- the present invention relates to a device for the treatment by means of gas of a large surface aluminum liquid bath maintained in the stationary state in an oven.
- aluminum is meant here both aluminum containing the usual impurities at rates which are a function of the quality treated, and the various alloys that this element is capable of forming.
- the word gas relates as well to simple elements such as nitrogen, argon and chlorine, for example, as to their mixtures.
- impurities are mainly constituted by hydrogen and metallic oxides such as alumina which come mainly from the pollution of the metal by the humidity of the environment to which other bodies and in particular other metals can be added, like magnesium for example, when aluminum comes from the remelting of waste.
- impurities will either form inclusions and cause defects in the cast products, or give them unwanted mechanical characteristics. It is therefore essential to treat the aluminum to get rid of these impurities before casting it.
- This treatment generally consists in introducing into the liquid metal bath, possibly in the presence of a flow, one or more reactive and / or inert gases, the former having the function of reacting with certain impurities, such as magnesium for example, the latter causing the impurities present initially or formed during the reactions towards the surface of the bath where they can be separated by skimming and filtration.
- This treatment can be carried out in ovens, whether it be alloy development ovens, holding ovens where the metal is in a stationary state and / or in pockets in which the metal flows continuously towards the stations of casting.
- rotary injectors are generally made of graphite, the only material capable of withstanding the abrasive action of the metal and the corrosive effect of chlorine at temperatures close to 800 ° C; but graphite is relatively fragile.
- a treatment device using gas from a bath (2) of liquid aluminum at rest in an oven (28) where it occupies an area at least equal to 10 m2 including a gantry (21) removable placed above the oven and to which hangs a set (1) of gas injection and mixing of the bath which plunges partly into the bath via an opening (3) which is formed in the vault (4) of the oven, said assembly comprising a rotary shaft (5) pierced along its axis by a cavity (6) closed downwards and opening above the oven in (7), said shaft being equipped at its upper part with '' a motor (17) and at its lower part a rotor (9) provided with blades (10) pierced with channels (11) connected to the cavity, device in which at the gantry are suspended at least three injection assemblies and of length greater than 2 meters, of vertical axis of symmetry which taken two by two are located in different planes, whose submerged parts are separated from each other only by the bath and that each of the trees is surrounded by a stator (13) extending downward
- the device according to the invention applies not to pockets of restricted surface where most often the metal circulates, but to ovens where the bath is stationary and occupies an area at least equal to 10 m2.
- ovens are generally closed on top and their vault is pierced with suitable openings through which the sets are introduced.
- a removable gantry a kind of metal frame which allows, by different mechanical means (pulleys, wheels, jacks, etc.) to move them horizontally from a waiting position to above the openings, simultaneously lower them into the bath and remove them after treatment of the metal.
- Each of the assemblies is connected to a motor intended to ensure the rotation of the injector and communicates by flexible tubes to the gas inlets.
- the movements of the gantry, the rotation speed of the motors and the adjustment of the gas flow rates are controlled from a cockpit which simultaneously manages the entire operating chain of the oven.
- the assemblies From the position point of view, the assemblies have their axes located two by two in different planes so as to obtain an offset and to avoid any alignment of more than two assemblies.
- the results of tests carried out with and without offset show that the liquid-gas exchange is better in the offset position.
- the gas injectors consist of a rotary shaft connected at its upper end to a drive motor and at its lower end to a rotor, a kind of disc provided on its side wall with blades.
- the shaft is pierced along its axis by a cavity which opens on its wall above the furnace and which is closed down and connected to channels which pass through the blades to open into the bath through the face not adjacent to the rotor. This cavity and these channels are used for the distribution of gas in the bath.
- stator which extends upwards above the furnace where it is fixed and downwards near the upper face of the rotor where it forms a relatively narrow space of a few millimeters so that the layer of metal therein acts as a hydrodynamic bearing for the rotor and facilitates the rotation of the latter.
- the lateral space which separates the stator from the rotor is filled with metal during the treatment and plays a damping role so that any "whip" effect on the rotor axis and any risk of breakage are eliminated.
- the measurement of this space is preferably between 10 and 30 mm.
- the injectors all rotate in the same direction to avoid eddies liable to hinder the rise of impurities on the surface.
- the axes With identical rotors, which is the most general case, it is preferable to place the axes at equal distances between them. These distances can vary between 2 and 6 times the value of the diameter of the rotors, which is generally between 100 and 500 mm in order to be within a range ensuring both a suitable dimension so as not to excessively multiply the number of injectors and compatible with the mechanical strength of trees.
- the range of rotational speeds enabling good dispersion to be obtained without resorting to excessive torques is between 150 and 600 revolutions / minute.
- the gas flow rate it is preferably between 6 and 12 m3 / h per injector, a lower flow unnecessarily lengthening the duration of the treatment and a higher flow resulting in the formation of too large bubbles which open on the surface of the bath without reacting.
- This gas is preferably distributed by four blades located in planes forming an angle between 3 and 10 degrees relative to the vertical, symmetrically distributed around the rotor and drilled horizontally throughout their width by a channel of diameter from 1 to 3 mm approximately which is connected on one side to the shaft cavity and which opens on the other side at the end of the blade.
- the rotor is preferably placed at a distance from the bottom of the oven between 1/4 and the 1/2 the height of the bath.
- the stator is preferably extended up to a distance from the upper face of the rotor of between 10 and 50 mm.
- FIG. 1 there is a gas injector assembly 1 which partially plunges into the bath 2 via an opening 3 formed in the roof 4 of the oven.
- This assembly comprises a rotary shaft 5 pierced along its axis by a cavity 6 opening below the furnace at 7 through which the next gas is brought 8.
- the shaft 5 is equipped at its lower part with a rotor 9 provided with blades 10 each pierced at their end by a channel 11 connected to the cavity 6 and which injects the gas into the next bath 12.
- the shaft 5 is surrounded by a stator 13 so as to leave a space 14 into which the bath enters.
- This stator extends downwards to a small distance from the face upper rotor to allow the bath to form an annular zone 15 acting as a hydrodynamic bearing; upwards the stator passes through the roof of the furnace to which it is suspended by a collar 16.
- the motor 17 ensures the rotation of the rotor via the shaft.
- FIG. 2 one can see a gantry 21 which rests on rails 22 by means of four wheels 23.
- This gantry is formed by an upper frame 24 to which the axes of the wheels are fixed, by four vertical uprights 25 and from the lower frame 26 removable along the uprights by means of a jack 27. From this lower frame are suspended the four gas injector assemblies 1 which plunge into the bath of the metal to be treated 2 contained in the furnace 28 according to offset positions the one in relation to the other.
- the gantry being in the waiting position A, and the lower frame in the high position, it is brought into position B located above the oven, then the lower frame is lowered to the intermediate position C where the elements are preheated before reaching position D where the elements are immersed in the bath. At this time, the injector engines are started and the gas is sent to the blades.
- the lower frame is gradually raised so as to drain the bath contained in the rotor-stator space. This frame being in high position B is then brought back to position A.
- a sample of metal thus treated was subjected to the telegas analysis method to determine the hydrogen content.
- the amount found was 0.10 ⁇ g / g of metal.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Coating With Molten Metal (AREA)
- Chemical Treatment Of Metals (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- ing And Chemical Polishing (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Claims (10)
- Vorrichtung zur Gasbehandlung eines flüssigen Aluminiumbades (2) in Ruhe in einem Ofen (28) wo es eine Oberfläche von wenigstens gleich 10 qm einnimmt, welche Vorrichtung eine abnehmbare Brücke (21) aufweist, die oberhalb des Ofens angeordnet ist und an der eine Einheit (1) zur Gasinjektion und zum Rühren des Bades aufgehängt ist, die teilweise in das Bad mit Hilfe einer im Gewölbe (4) des Ofens angebrachten Öffnung (3) eintaucht und eine Drehwelle (5) aufweist, die längs ihrer Achse von einem Hohlraum (6) durchbohrt ist, der nach unten geschlossen ist und oberhalb des Ofens bei (7) mündet, welche Welle an ihrem oberen Teil mit einem Motor (17) und an ihrem unteren Teil mit einem Rotor (9) bestückt ist, der mit von Kanälen (11) durchbohrten Flügeln (10) ausgerüstet und an den Hohlraum angeschlossen ist, wobei in der Vorrichtung an der Brücke wenigstens drei Injektions- und Rühreinheiten einer Länge über 2 Meter und vertikaler Symmetrieachse aufgehängt sind, von denen je zwei in verschiedenen Ebenen liegen und deren eingetauchte Teile untereinander nur durch das Bad getrennt sind, und wobei jede der Wellen von einem Stator (13 umgeben ist, der sich nach unten bis nahe der Oberseite des Rotors und nach oben oberhalb des Gewölbes erstreckt.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnete, daß sich die Wellen alle in der gleichen Richtung drehen.
- Verwendung der Vorrrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß die Achsen der Wellen untereinander gleiche Abstände haben.
- Verwendung der Vorrichtung nach dem Anspruch 1, daruch gekennzeichnet, daß die Achsen untereinander durch einen Abstand im Bereich vom 2- bis 6-fachen des Durchmessers der Rotoren getrennt sind.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß die Rotoren einen Durchmesser im Bereich von 100 bis 500 mm haben.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß die Drehgeschwindigkeit der Rotoren im Bereich von 150 bis 600 U/min ist.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß der Gasdurchsatz im Bereich von 6 bis 12 m³/h je Injektor ist.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß die Flügel in Ebenen liegen, die mit der Vertikalen einen Winkel im Bereich von 3 bis 10 Grad bilden.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß der Rotor in einem Abstand im Bereich von 1/4 bis 1/2 der Höhe des Bades vom Boden des Ofens angeordnet ist.
- Verwendung der Vorrichtung nach dem Anspruch 1, dadurch gekennzeichnet, daß das Unterende des Stators in einem Abstand im Bereich von 10 bis 50 mm von der Oberkante des Rotors angeordnet ist.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT90420406T ATE103992T1 (de) | 1989-09-20 | 1990-09-17 | Begasungsvorrichtung fuer ein stationaeres aluminium-schmelzbad mit grosser oberflaeche. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8912540 | 1989-09-20 | ||
FR8912540A FR2652018B1 (fr) | 1989-09-20 | 1989-09-20 | Dispositif de traitement au moyen de gaz d'un bain liquide d'aluminium de grande surface maintenu a l'etat stationnaire dans un four. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0419378A1 EP0419378A1 (de) | 1991-03-27 |
EP0419378B1 true EP0419378B1 (de) | 1994-04-06 |
Family
ID=9385802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90420406A Expired - Lifetime EP0419378B1 (de) | 1989-09-20 | 1990-09-17 | Begasungsvorrichtung für ein stationäres Aluminium-Schmelzbad mit grosser Oberfläche |
Country Status (9)
Country | Link |
---|---|
US (1) | US5028035A (de) |
EP (1) | EP0419378B1 (de) |
AT (1) | ATE103992T1 (de) |
AU (1) | AU621531B2 (de) |
CA (1) | CA2023753C (de) |
DE (1) | DE69007921T2 (de) |
ES (1) | ES2050989T3 (de) |
FR (1) | FR2652018B1 (de) |
NO (1) | NO176925C (de) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2645456B1 (fr) * | 1989-04-11 | 1994-02-11 | Air Liquide | Procede et installation de traitement d'un liquide avec un gaz |
US5160693A (en) * | 1991-09-26 | 1992-11-03 | Eckert Charles E | Impeller for treating molten metals |
US6056803A (en) * | 1997-12-24 | 2000-05-02 | Alcan International Limited | Injector for gas treatment of molten metals |
US9127332B2 (en) * | 2008-03-11 | 2015-09-08 | Pyrotek, Inc. | Molten aluminum refining and gas dispersion system |
CN110607461B (zh) * | 2018-11-16 | 2023-05-09 | 柳州职业技术学院 | 一种铝合金精炼用长效复合式石墨搅拌装置及制备方法 |
CN117701893B (zh) * | 2024-02-01 | 2024-04-26 | 北京航空航天大学 | 一种合金熔体旋转喷吹精炼装置及方法 |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1635037A (en) * | 1925-09-28 | 1927-07-05 | Edwards John | Means for agitating and stirring molten metal in open-hearth and like furnaces |
US3227547A (en) * | 1961-11-24 | 1966-01-04 | Union Carbide Corp | Degassing molten metals |
US3703340A (en) * | 1970-10-09 | 1972-11-21 | Us Reduction Co | Mechanical puddler |
US3743263A (en) * | 1971-12-27 | 1973-07-03 | Union Carbide Corp | Apparatus for refining molten aluminum |
US3870511A (en) * | 1971-12-27 | 1975-03-11 | Union Carbide Corp | Process for refining molten aluminum |
AT336900B (de) * | 1974-04-04 | 1977-05-25 | Vmw Ranshofen Berndorf Ag | Vorrichtung zur einbringung von gasen in flussigkeiten, insbesondere schmelzen |
AT330470B (de) * | 1974-07-17 | 1976-07-12 | Vmw Ranshofen Berndorf Ag | Begasungsvorrichtung fur metallurgische gefasse, insbesondere schmelzofen |
US4203581A (en) * | 1979-03-30 | 1980-05-20 | Union Carbide Corporation | Apparatus for refining molten aluminum |
US4327901A (en) * | 1980-03-10 | 1982-05-04 | Kaiser George S | Melt and hold furnace for non-ferrous metals |
FR2514370B1 (fr) * | 1981-10-14 | 1989-09-29 | Pechiney Aluminium | Dispositif pour le traitement, au passage, d'un courant de metal ou alliage liquide a base d'aluminium ou de magnesium |
FR2568267B1 (fr) * | 1984-07-27 | 1987-01-23 | Pechiney Aluminium | Poche de chloruration d'alliages d'aluminium destinee a eliminer le magnesium |
JPS62205235A (ja) * | 1986-03-05 | 1987-09-09 | Showa Alum Corp | 溶融金属の処理装置 |
JP2505525B2 (ja) * | 1988-04-08 | 1996-06-12 | 三菱重工業株式会社 | スラリ―の気液接触処理装置 |
US4884786A (en) * | 1988-08-23 | 1989-12-05 | Gillespie & Powers, Inc. | Apparatus for generating a vortex in a melt |
IL93349A0 (en) * | 1989-02-17 | 1990-11-29 | Carborundum Co | Method and apparatus for injecting gas into molten metal |
-
1989
- 1989-09-20 FR FR8912540A patent/FR2652018B1/fr not_active Expired - Fee Related
-
1990
- 1990-07-13 US US07/551,905 patent/US5028035A/en not_active Expired - Lifetime
- 1990-08-07 NO NO903464A patent/NO176925C/no unknown
- 1990-08-23 CA CA002023753A patent/CA2023753C/fr not_active Expired - Fee Related
- 1990-09-07 AU AU62303/90A patent/AU621531B2/en not_active Ceased
- 1990-09-17 AT AT90420406T patent/ATE103992T1/de active
- 1990-09-17 DE DE69007921T patent/DE69007921T2/de not_active Expired - Fee Related
- 1990-09-17 EP EP90420406A patent/EP0419378B1/de not_active Expired - Lifetime
- 1990-09-17 ES ES90420406T patent/ES2050989T3/es not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DE69007921T2 (de) | 1994-10-06 |
EP0419378A1 (de) | 1991-03-27 |
DE69007921D1 (de) | 1994-05-11 |
CA2023753C (fr) | 1997-10-07 |
US5028035A (en) | 1991-07-02 |
FR2652018B1 (fr) | 1994-03-25 |
NO903464L (no) | 1991-03-21 |
AU6230390A (en) | 1991-03-28 |
CA2023753A1 (fr) | 1991-03-21 |
NO176925B (no) | 1995-03-13 |
ATE103992T1 (de) | 1994-04-15 |
AU621531B2 (en) | 1992-03-12 |
NO903464D0 (no) | 1990-08-07 |
ES2050989T3 (es) | 1994-06-01 |
FR2652018A1 (fr) | 1991-03-22 |
NO176925C (no) | 1995-06-21 |
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