EP0062548B1 - Process for gas-stirring a metal bath - Google Patents
Process for gas-stirring a metal bath Download PDFInfo
- Publication number
- EP0062548B1 EP0062548B1 EP82400345A EP82400345A EP0062548B1 EP 0062548 B1 EP0062548 B1 EP 0062548B1 EP 82400345 A EP82400345 A EP 82400345A EP 82400345 A EP82400345 A EP 82400345A EP 0062548 B1 EP0062548 B1 EP 0062548B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- bath
- stirring
- inert gas
- nitrogen
- fluid
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/30—Regulating or controlling the blowing
- C21C5/35—Blowing from above and through the bath
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D1/00—Treatment of fused masses in the ladle or the supply runners before casting
- B22D1/002—Treatment with gases
- B22D1/005—Injection assemblies therefor
-
- 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
Definitions
- the present invention relates to the pneumatic mixing of a metal bath. It applies more particularly to the stirring of a bath of cast iron during refining in a converter to oxygen blown from above.
- the fluid used is generally a chemically inert gas vis-à-vis the bath, such as argon -or preferably nitrogen due to its very low cost price.
- the object of the present invention is to achieve high mixing gas flow rates while avoiding the difficulties encountered in known practices.
- the subject of the invention is a process for pneumatically stirring a metal bath contained in a crucible, according to which a stirring agent consisting, at least, is injected through permeable refractory elements mounted in the bottom of the crucible. temporarily, with an organic fluid and characterized in that said fluid is a hydrocarbon in the liquid state.
- liquid is meant an organic fluid in the liquid state under standard temperature and pressure conditions or easily liquefiable under low pressure, in this case under a pressure lower than the injection pressure in the permeable elements. (3 to 6 bars approximately).
- a brewing fluid consisting of an organic liquid, for example propane, then, some time before the desired end of brewing - for example a few minutes before - the organic liquid is replaced by an inert gas, such as nitrogen or argon, depending on the maximum allowable nitrogen contents for the target shade.
- an inert gas such as nitrogen or argon
- stirring with inert gas provides a "washing" of the bath, which is thus freed from the dissolved hygrogen accumulated during initial stirring by the injection of organic liquid.
- This particular implementation of the invention is entirely suitable for refining cast iron by conversion to oxygen with stirring with argon or nitrogen.
- the invention therefore provides an efficient stirring of the bath during the refining process and this without risk of pollution of the metal by both hydrogen and nitrogen.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Treating Waste Gases (AREA)
- Catalysts (AREA)
- Manufacture Of Alloys Or Alloy Compounds (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
- Soy Sauces And Products Related Thereto (AREA)
Abstract
Description
La présente invention concerne le brassage pneumatique d'un bain métallique. Elle s'applique plus particulièrement au brassage d'un bain de fonte en cours d'affinage dans un convertisseur à l'oxygène soufflé par le haut.The present invention relates to the pneumatic mixing of a metal bath. It applies more particularly to the stirring of a bath of cast iron during refining in a converter to oxygen blown from above.
Il est connu d'étendre les possibilités métallurgiques des techniques d'affinage à l'oxygène soufflé par le haut en brassant le bain par un fluide à l'état gazeux injecté au travers d'éléments réfractaires perméables logés dans le fond du convertisseur (certificat d'utilité français No. 2322202 - IRSID, brevet luxembourgeois No. 42419 - CNRM).It is known to extend the metallurgical possibilities of refining techniques with oxygen blown from above by stirring the bath with a gaseous fluid injected through permeable refractory elements housed in the bottom of the converter (certificate French utility No. 2322202 - IRSID, Luxembourg patent No. 42419 - CNRM).
Le fluide utilisé est généralement un gaz chimiquement inerte vis-à-vis du bain, comme l'argon -ou de préférence, l'azote en raison de son très faible coût de revient.The fluid used is generally a chemically inert gas vis-à-vis the bath, such as argon -or preferably nitrogen due to its very low cost price.
Cette nouvelle technique, dont les récents développements l'ont portée à la connaissance du public sous la dénomination de Procédé «LBE» (Lance-Brassage-Equilibre), tend, comme son nom l'indique, à réaliser l'équilibre entre le métal et le laitier, permettant ainsi de comuler les avantages respectifs des procédés classiques d'affinage à soufflage d'oxygène par le haut et à soufflage d'oxygène par le bas. Cette technique se traduit notamment par un meilleur contrôle de la conduite des opérations d'affinage en procurant une plus grande souplesse tant dans le choix du moment, que de la durée ou, dans une certaine mesure, de l'intensité de l'injection gazeuse.This new technique, whose recent developments have brought it to the attention of the public under the name of “LBE” Process (Lance-Brassage-Equilibre), tends, as its name suggests, to achieve balance between metal and slag, thereby allowing the respective advantages of the conventional top-blown and bottom-blown oxygen refining processes to be offset. This technique results in particular in better control of the conduct of refining operations by providing greater flexibility both in the choice of the time, as well as the duration or, to a certain extent, the intensity of the gas injection. .
Elle se heurte cependant à des contraintes technologiques qui limitent les possibilités d'introduire par élément une quantité de gaz aussi importante qu'un le voudrait.However, it encounters technological constraints which limit the possibilities of introducing as much gas per element as one would like.
Il a déjà été proposé de remplacer le gaz de brassage à injecter par un gaz liquéfié se vaporisant au contact du bain. On a ainsi pu obtenir, à débit unitaire donné des volumes de gaz de brassage beaucoup plus importants (EP-A-0032343 - IRSID).It has already been proposed to replace the stirring gas to be injected with a liquefied gas vaporizing on contact with the bath. It was thus possible to obtain, at a given unit flow rate, much larger mixing gases (EP-A-0032343 - IRSID).
Toutefois, il est apparu que, selon le type d'éléments perméables utilisés, ces derniers tenaient plus au moins bien aux chocs thermiques causés par des injections répétitives de fluide cryogénique.However, it appeared that, depending on the type of permeable elements used, the latter were more or less resistant to thermal shocks caused by repetitive injections of cryogenic fluid.
Le but de la présente invention est de parvenir à des débits de gaz de brassage importants tout en évitant les difficultés rencontrées dans les pratiques connues.The object of the present invention is to achieve high mixing gas flow rates while avoiding the difficulties encountered in known practices.
A cet effet, l'invention a pour objet un procédé de brassage pneumatique d'un bain métallique contenu dans un creuset, selon lequel on injecte au travers d'éléments réfractaires perméables montés dans le fond du creuset un agent de brassage constitué, au moins temporairement, par un fluide organique et caractérisé en ce que ledit fluide est un hydrocarbure à l'état liquide.To this end, the subject of the invention is a process for pneumatically stirring a metal bath contained in a crucible, according to which a stirring agent consisting, at least, is injected through permeable refractory elements mounted in the bottom of the crucible. temporarily, with an organic fluid and characterized in that said fluid is a hydrocarbon in the liquid state.
Par «liquide», il faut entendre un fluide organique à l'état liquide dans les conditions standard de température et de pression ou facilement liquéfiable sous faible pression, en l'occurrence sous une pression inférieure à la pression d'injection dans les éléments perméables (3 à 6 bars environ).By “liquid” is meant an organic fluid in the liquid state under standard temperature and pressure conditions or easily liquefiable under low pressure, in this case under a pressure lower than the injection pressure in the permeable elements. (3 to 6 bars approximately).
Dans le cas d'hydrocarbures aliphatiques saturés les plus courants, il s'agit donc de ceux de la famille Cn Hzn+2 où n est égal ou supérieur à 3 (propane, butane, etc.).In the case of the most common saturated aliphatic hydrocarbons, these are therefore those of the family C n H zn + 2 where n is equal to or greater than 3 (propane, butane, etc.).
On bénéficie de cette façon des avantages liés à une injection d'un fluide de brassage à l'état liquide sans pour autant soumettre les éléments réfractaires perméables à des chocs thermiques préjudiciables à leur tenue.In this way, the advantages linked to an injection of a stirring fluid in the liquid state are obtained without subjecting the refractory elements permeable to thermal shocks detrimental to their behavior.
Il est d'ailleurs possible, conformément à une variante de mise en oeuvre préférée de l'invention, d'éliminer tout risque de ce genre simplement en préchauffant le liquide organique avant de l'injecter.It is also possible, in accordance with a preferred implementation variant of the invention, to eliminate any risk of this kind simply by preheating the organic liquid before injecting it.
Par ailleurs, l'invention présente d'autres intérêts parmi lesquels on peut notamment mentionner:
- - une protection des éléments réfractaires perméables et des régions avoisinantes par dépôt d'une couche de carbone de décomposition du liquide organique injecté,
- - l'absence de tout risque de nitruration du bain. On connait en effet les difficultés que l'on a pour éliminer l'azote d'un bain métallique brassé à l'aide de ce gaz.
- - protection of permeable refractory elements and surrounding regions by depositing a layer of carbon decomposing the injected organic liquid,
- - the absence of any risk of nitriding the bath. We know in fact the difficulties we have in removing nitrogen from a metal bath stirred with this gas.
Il doit être cependant noté que l'utilisation d'un fluide organique peut entraîner une certaine hydrogénation du bain qui, dans certains cas, peut être indésirable.It should be noted, however, that the use of an organic fluid may cause some hydrogenation of the bath which, in some cases, may be undesirable.
Conformément à une mise en oeuvre de l'invention, il est possible de surmonter cette difficulté.In accordance with an implementation of the invention, it is possible to overcome this difficulty.
Pour ce faire, on commence par injecter un fluide de brassage constitué par un liquide organique, par exemple du propane, puis, quelques temps avant la fin souhaitée du brassage - par exemple quelques minutes avant - on remplace le liqide organique par un gaz inerte, tel que l'azote ou l'argon, suivant les teneurs en azote maximales admissibles pour la nuance visée.To do this, we start by injecting a brewing fluid consisting of an organic liquid, for example propane, then, some time before the desired end of brewing - for example a few minutes before - the organic liquid is replaced by an inert gas, such as nitrogen or argon, depending on the maximum allowable nitrogen contents for the target shade.
De cette façon, le brassage au gaz inerte procure un «lavage» du bain, lequel se trouve ainsi débarrassé de l'hygrogène dissous accumulé lors de brassage initial par l'injection du liquide organique.In this way, stirring with inert gas provides a "washing" of the bath, which is thus freed from the dissolved hygrogen accumulated during initial stirring by the injection of organic liquid.
Cette mise en oeuvre particulière de l'invention est tout-à-fait indiquée pour l'affinage de la fonte par conversion à l'oxygène avec brassage à l'argon ou à l'azote.This particular implementation of the invention is entirely suitable for refining cast iron by conversion to oxygen with stirring with argon or nitrogen.
Dans ce cas, le moment où l'on passe de l'injection du liquide organique à celle de l'azote doit être au plus tôt, la fin de la décarburation du bain. En effet, ce n'est qu'à partir de la fin de la période de décarburation que les conditions métallurgiques deviennent nettement défavorables pour une dissolution de l'azote, de sorte que le choix de cet élément en tant que gaz de brassage en aval de la décarburation du bain, n'entraîne aucune nitruration excessive de ce dernier, du moins dans les tolérances habituellement admises.In this case, the moment when one passes from the injection of the organic liquid to that of the nitrogen must be at the earliest, the end of the decarburization of the bath. Indeed, it is only from the end of the decarburization period that the metallurgical conditions become clearly unfavorable for a dissolution of the nitrogen, so that the choice of this element as downstream mixing gas decarburization of the bath, does not cause excessive nitriding of the latter, at least within the tolerances usually accepted.
Dans cette forme de mise en oeuvre, l'invention procure donc un brassage efficace du bain durant le processus d'affinage et ceci sans risque de pollution du métal tant par l'hydrogène que par l'azote.In this embodiment, the invention therefore provides an efficient stirring of the bath during the refining process and this without risk of pollution of the metal by both hydrogen and nitrogen.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT82400345T ATE13075T1 (en) | 1981-03-11 | 1982-03-01 | METHOD OF GAS STIRRING IN A METAL BATH. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8105017 | 1981-03-11 | ||
FR8105017A FR2501722B1 (en) | 1981-03-11 | 1981-03-11 | PROCESS FOR THE PNEUMATIC BREWING OF A METAL BATH |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0062548A1 EP0062548A1 (en) | 1982-10-13 |
EP0062548B1 true EP0062548B1 (en) | 1985-05-02 |
Family
ID=9256183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP82400345A Expired EP0062548B1 (en) | 1981-03-11 | 1982-03-01 | Process for gas-stirring a metal bath |
Country Status (8)
Country | Link |
---|---|
US (1) | US4397684A (en) |
EP (1) | EP0062548B1 (en) |
JP (1) | JPS57161019A (en) |
AT (1) | ATE13075T1 (en) |
AU (1) | AU8055582A (en) |
CA (1) | CA1175236A (en) |
DE (1) | DE3263349D1 (en) |
FR (1) | FR2501722B1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2545393B1 (en) * | 1983-05-04 | 1985-09-06 | Air Liquide | PROCESS FOR PRODUCING SOLID METAL PARTICLES FROM A METAL BATH |
SE8702338L (en) * | 1987-06-05 | 1988-12-06 | Aga Ab | GAS RINSE OF MELMA IN SHAENK |
GB2255983A (en) * | 1991-05-24 | 1992-11-25 | Mexicano Investigacion | Stirring metal melts with methane. |
JP2002286602A (en) * | 2001-03-22 | 2002-10-03 | Matsushita Electric Ind Co Ltd | Method and device for stirring solution, sample cell using the device, and solution consistency measuring instrument using the same |
CN101892356B (en) * | 2010-07-21 | 2012-05-30 | 中国重型机械研究院有限公司 | Argon blowing protection system |
CN112626350B (en) * | 2020-12-16 | 2021-11-30 | 东北大学 | Device and method for deeply purifying aluminum-lithium alloy melt |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0032343A1 (en) * | 1980-01-02 | 1981-07-22 | INSTITUT DE RECHERCHES DE LA SIDERURGIE FRANCAISE (IRSID) France | Method for the gaseous stirring of a molten metal bath |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US42419A (en) * | 1864-04-19 | Petefls | ||
BE609232A (en) * | 1961-10-16 | 1962-04-16 | Centre Nat Rech Metall | Improvements to cast iron refining processes |
FR90350E (en) * | 1965-10-21 | 1967-11-24 | Air Liquide | Process for treating liquid metals, applicable in particular to the production of nodular cast iron |
BE752893A (en) * | 1969-07-08 | 1970-12-16 | Forges De La Loire St Chamond | METHOD AND DEVICE FOR COOLING A REFINING CONVERTER TUBE |
DE2147717A1 (en) * | 1971-09-24 | 1973-03-29 | Kloeckner Werke Ag | Steel refining - using liquid coolant blown into melt together with oxygen through two-component blast-pipe |
US3854932A (en) * | 1973-06-18 | 1974-12-17 | Allegheny Ludlum Ind Inc | Process for production of stainless steel |
FR2322202A1 (en) * | 1975-08-29 | 1977-03-25 | Siderurgie Fse Inst Rech | Steel refining by oxygen lancing and bottom blowing - for improved quality steel of various grades |
LU82069A1 (en) * | 1980-01-09 | 1981-09-10 | Arbed | METHOD FOR REFINING A METAL BATH |
-
1981
- 1981-03-11 FR FR8105017A patent/FR2501722B1/en not_active Expired
-
1982
- 1982-02-17 AU AU80555/82A patent/AU8055582A/en not_active Abandoned
- 1982-03-01 DE DE8282400345T patent/DE3263349D1/en not_active Expired
- 1982-03-01 EP EP82400345A patent/EP0062548B1/en not_active Expired
- 1982-03-01 AT AT82400345T patent/ATE13075T1/en active
- 1982-03-04 US US06/354,912 patent/US4397684A/en not_active Expired - Fee Related
- 1982-03-09 JP JP57035951A patent/JPS57161019A/en active Pending
- 1982-03-09 CA CA000397930A patent/CA1175236A/en not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0032343A1 (en) * | 1980-01-02 | 1981-07-22 | INSTITUT DE RECHERCHES DE LA SIDERURGIE FRANCAISE (IRSID) France | Method for the gaseous stirring of a molten metal bath |
Also Published As
Publication number | Publication date |
---|---|
FR2501722A1 (en) | 1982-09-17 |
AU8055582A (en) | 1982-09-16 |
CA1175236A (en) | 1984-10-02 |
ATE13075T1 (en) | 1985-05-15 |
FR2501722B1 (en) | 1986-08-14 |
DE3263349D1 (en) | 1985-06-05 |
US4397684A (en) | 1983-08-09 |
EP0062548A1 (en) | 1982-10-13 |
JPS57161019A (en) | 1982-10-04 |
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