EP1541699A1 - Method for feeling steel - Google Patents
Method for feeling steel Download PDFInfo
- Publication number
- EP1541699A1 EP1541699A1 EP02768214A EP02768214A EP1541699A1 EP 1541699 A1 EP1541699 A1 EP 1541699A1 EP 02768214 A EP02768214 A EP 02768214A EP 02768214 A EP02768214 A EP 02768214A EP 1541699 A1 EP1541699 A1 EP 1541699A1
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- EP
- European Patent Office
- Prior art keywords
- gas
- pan
- steel
- metal
- blowing
- 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.)
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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
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- 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
-
- 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
- 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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/06—Constructional features of mixers for pig-iron
-
- 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
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/0075—Treating in a ladle furnace, e.g. up-/reheating of molten steel within the ladle
-
- 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
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/072—Treatment with gases
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- 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
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- 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
- F27D3/18—Charging particulate material using a fluid carrier
-
- 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
- F27D2027/002—Gas stirring
Definitions
- the invention relates to methods for the treatment of liquid metal in a pan outside the furnace in black metallurgy.
- the intensification of the stirring process of the metal which is a reduction
- the steelworking time has an important meaning in the process treating metal outside the oven in a pan.
- the Homogenization of the melt accelerates the processes of calming and the disposal of non-metallic inclusions, as well as desulphurisation and Dephosphorization of the steel, which is the achievement of the objectives of ladle metallurgy guaranteed.
- a method for intensifying the stirring of metal in a pan by increasing the gas flow rate for blowing leads the gas through a blow mold of the type "hollow Stopper rod "and to avoid splashing of metal at elevated Gas supply is used a disc-shaped front part (screen) on the Stopper rod (see, e.g., Stahl, No. 12, 1999, pp. 17-19).
- the main disadvantage of the method is the attempt to complete the task of Intensify the stirring of the metal by increasing the gas supply to solve. Moreover, in this case, most of the metal in the pan is not from the stirring comprises, in particular not in their soil zones. All in all reduces the above mentioned the effectiveness of the known method in the Solution of the task.
- the main drawback of this process is the high cost of used equipment with a relatively low stirring effect.
- a gas or gas-powder mixture through arranged in the lower part of the molten bath Blowing devices, of which at least one is offset from the middle of the pan.
- the supply of Gas or gas-powder mixture through special plugs in the bottom of the pan is preferred, its implementation concludes the supply of the specified Components by a submerged tuyere (tuyeres) is not enough.
- the known method has a significant disadvantage: in the course of Blowing the steel by means of the gas / gas powder mixture is the Metal stirred unevenly over the pan volume. Especially the im Entry path of the gas / gas powder mixture in the steel areas (most active zone) of the liquid metal become an intense stirring motion subjected. When approaching the gas / gas powder mixture to the Surface of the metal in the pan widen these areas, flow through (reducing speed) the upper layers of the Melting bath and sink from the surface as weakened descending Streams down. Of course, this portrayed image reduces that Movement of stirred metal efficiency of stirring of steel because it the entire volume of metal in the pan and especially the bottom zones of the Melting bath detected very slowly. Altogether the posed task of the Acceleration of the homogenization of the metal composition is not achieved.
- the known process requires increased use of gas and in particular in time, which in the current technological manufacturing process of steel in the essential is not sufficiently available.
- the inventive method for stirring metal in a pan does not have the mentioned disadvantages.
- the active zone the detection of the metal volume by the gas / gas powder mixture significantly widened. This leads to the reduction of the time to reach a homogenized metal composition without increasing the supplied Amount of gas, i. the technical task of intensifying the stirring of steel in a pan by blowing a gas / gas powder mixture solved.
- a method of stirring steel in a pan comprising blowing of the steel from below by means of a gas / gas powder mixture through at least two provided blowing devices, which are diametrically are arranged opposite sides of the pan, according to the invention the blowing through alternately first by one of the blowing devices, the on one side of the pan, and then the other Blowing device, which is located on the other side of the pan, takes place.
- the blowing device which does not blow through at the moment, a pressure which precludes the inflow of metal into this device.
- the Period of the operation change between the blowing devices is increased with the increase in steel mass in the pan.
- the volume of the supplied Gas is at the switching of the supply of gas or gas-powder mixture from one blowing device to the other left unchanged.
- a pan is shown with metal, in the two Blowing devices are provided as a plug in the pan bottom.
- Fig. 2 is an analogue pan with two blowing devices in the form of tuyeres shown.
- Fig. 3 the view in the direction of arrow A gem.
- Fig. 1 shown.
- Fig. 4 shows the view in the direction of arrow A gem.
- the pan has at least two blowing devices.
- the ladle 1 is filled with the liquid steel 2. in the The bottom of the ladle (Fig. 1) are on diametrically opposite sides of the pan 1 (Fig. 3) at least two blowing devices 3 are provided. The number of these Devices can be higher, but must be straight. In the pan 1 can on blow molds 4 arranged diametrically opposite sides of the pan 1 be provided. The number of blow molds may be higher but must be even.
- the Gas or gas powder mixture 5 is the pan by plugging in each case Pan base (Fig. 1) or tuyeres 4 (Fig. 2). The gas or the Gas-powder mixture can be fed to the pan separately. In this Case increases the number of devices 3 (blow molding 4) to the next even number. In Fig.
- the method of stirring steel in a pan is as follows carried out.
- the steel 2 is poured.
- the for the doping, Desulfurization and dephosphorization of the steel necessary elements become by known methods or as a powder by the described Devices 3 (or 4), or by both methods simultaneously in the steel introduced.
- the result is formed in the Melt the main currents, which are represented by the lines 6.
- the stopper 3 (in the tuyere 4) on the opposite Side of the pan held a gas pressure, which is the inflow of steel into these excludes.
- the direction of the Main flows of the metal in the pan bath by supply of the gas (gas-powder mixture) 5 through the plug 3 (blow mold 4), on the opposite Side of the pan is arranged (in Fig.
- a "cold model" of a pan 1 had the one shown in Fig. 1 Dimensions.
- the pan was tap water 2 up to the height of 430 mm filled.
- the pan was equipped with three platinum electrodes: one in the bottom Part of the pan (distance from the water level 370 mm), one in the middle part of the Pan (distance from the water level 220 mm) and one in the upper part of the pan (Distance from the water level 60 mm), the advance in the areas tap water - 0.1 wt.% Aqueous KCl solution were calibrated. All three electrodes were 55 mm away from the inner wall of the pan model. There was also one portable electrode provided with the addition of the homogenization of the Solution in the centers of the pan model, in the bottom part, at the Water surface, as well as in the joints of the floor and the walls of the pan was evaluated.
- a 20% KCI concentrate was prepared and in a thin Rubber balloon on the bottom of the pan model in the area near the Pan wall, which was located 90 ° from the devices 3, lowered. Of the Balloon was cut up. It was by the 20% KCl concentrate after its uniform distribution over the body of water a concentration of 0, 1% KCl set in the water, on which the electrodes were calibrated. The Use of the balloon has a minimal disruptive effect on the balloon Water bath guaranteed.
- the gas (air) was absorbed by the devices in the soil in an amount supplied from 6 l / min.
- Example 1 Under the conditions given in Example 1 was a alternating air supply with a period of 30 sec. performed. In which Change in direction was the amount of air supplied at 6 l / min. held. After 35 min, the pan model became a homogeneous solution with the above Receive concentration, i. the stirring time was 2.4 times compared to Example 1 reduced.
- Example 1 Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 20 sec. performed. To 60 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.4 times compared to Example 1. At the end of the 60-minute stirring, there were zones in the water volume larger and smaller concentrations than 0.1% KCl detected in water were not registered by the main electrodes.
- Example 1 Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 10 sec. performed. After 84 - 87 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time became practical in comparison with Example 1 maintained. At the end of the stirring were in the water volume zones with larger and smaller concentrations than 0, 1% KCl detected in water, the were not registered by the main electrodes.
- Example 1 Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 40 sec. performed. To 55 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.5 times compared to Example 1. The water volume lacked zones with a KCI concentration that differed from the Concentration of 0.1 wt.% KCl difference.
- Example 1 Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 50 sec. performed. To 60 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.4 times compared to Example 1. The water volume lacked zones with a KCI concentration that differed from the Concentration of 0.1 wt.% KCI distinguished.
- the inventive method for stirring steel in a pan allows a substantial intensification by a simple process management the stirring of the steel (a reduction in the time to carry out) without a loss of stirring quality.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Furnace Details (AREA)
- Paper (AREA)
- Heat Treatment Of Steel (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
Die Erfindung bezieht sich auf Verfahren zur Behandlung flüssigen Metalls in einer Pfanne außerhalb des Ofens in der Schwarzmetallurgie.The invention relates to methods for the treatment of liquid metal in a pan outside the furnace in black metallurgy.
Es ist bekannt, dass bei der Behandlung von Stahl außerhalb des Ofens Inertgas und technologische Pulver in die Schmelze entweder durch in die Schmelze eingetauchte Blasformen oder durch spezielle im Pfannenboden angeordnete Stopfen zugeführt werden.It is known that in the treatment of steel outside the furnace Inert gas and technological powder in the melt either through in the Melt submerged blow molds or by special in the pan bottom arranged plugs are supplied.
Die Intensivierung des Rührvorgangs des Metalls, welche eine Reduktion der Zeit der Stahlbearbeitung ermöglicht, hat eine wichtige Bedeutung im Prozeß der Behandlung von Metall außerhalb des Ofens in einer Pfanne. Die Homogenisierung der Schmelze beschleunigt die Vorgänge der Beruhigung und der Beseitigung nichtmetallischer Einschlüsse, sowie der Desulfurierung und Entphosphorung des Stahls, was die Erreichung der Ziele der Pfannenmetallurgie gewährleistet.The intensification of the stirring process of the metal, which is a reduction The steelworking time has an important meaning in the process treating metal outside the oven in a pan. The Homogenization of the melt accelerates the processes of calming and the disposal of non-metallic inclusions, as well as desulphurisation and Dephosphorization of the steel, which is the achievement of the objectives of ladle metallurgy guaranteed.
Bekannt ist ein Verfahren zur Intensivierung des Rührens von Metall in einer Pfanne durch Erhöhung des Gasdurchsatzes für das Durchblasen. Im bekannten Verfahren führt man das Gas durch eine Blasform vom Typ "hohle Stopfenstange" zu und zur Vermeidung des Verspritzens von Metall bei erhöhter Gaszufuhr verwendet man ein scheibenförmiges Stirnteil (Schirm) an der Stopfenstange (siehe, z.B., Stahl, Nr. 12, 1999, S. 17-19).A method is known for intensifying the stirring of metal in a pan by increasing the gas flow rate for blowing. in the known method leads the gas through a blow mold of the type "hollow Stopper rod "and to avoid splashing of metal at elevated Gas supply is used a disc-shaped front part (screen) on the Stopper rod (see, e.g., Stahl, No. 12, 1999, pp. 17-19).
Der Hauptnachteil des Verfahrens ist der Versuch, die Aufgabe der Intensivierung des Rührens des Metalls durch Erhöhung der Gaszufuhr zu lösen. Außerdem wird in diesem Fall der größte Teil des Metalls in der Pfanne nicht von der Rührbewegung umfaßt, insbesondere nicht in ihren Bodenzonen. Insgesamt reduziert das oben Angeführte die Effektivität des bekannten Verfahrens bei der Lösung der gestellten Aufgabe.The main disadvantage of the method is the attempt to complete the task of Intensify the stirring of the metal by increasing the gas supply to solve. Moreover, in this case, most of the metal in the pan is not from the stirring comprises, in particular not in their soil zones. All in all reduces the above mentioned the effectiveness of the known method in the Solution of the task.
Weiterhin bekannt ist ein Verfahren zum Rühren von Stahl in einer Pfanne, umfassend die Einführung eines löslichen Gases in den Stahl, das sich bei Vakuumbehandlung in Form kleinster auf die Schmelzbadoberfläche aufschwimmender Blasen im Stahl (wie auch in Sodawasser) abscheidet (siehe, z.B., "Stahlerzeugung an der Schwelle des dritten Jahrtausends", Anlage 7 zur Zeitschrift "Neuigkeiten der Schwarzmetallurgie im Ausland", 2000, S. 25).Also known is a method for stirring steel in a pan, including the introduction of a soluble gas into the steel, which is at Vacuum treatment in the form of the smallest on the melt surface Floating bubbles in the steel (as well as in soda water) separates (see For example, "Steelmaking on the Threshold of the Third Millennium", Annex 7 to the Journal "News of Black Metallurgy Abroad", 2000, p. 25).
Der Hauptnachteil des bekannten Verfahrens liegt in seiner offensichtlichen Verteuerung, u.a. wegen der Notwendigkeit, eine Umlaufvakuumbehandlung einzusetzen (NK-PERM-Prozess der Firma "Nippon Kokan").The main disadvantage of the known method lies in its obvious More expensive, u.a. because of the need for a recirculating vacuum treatment (NK-PERM process of the company "Nippon Kokan").
Bekannt ist auch ein Verfahren zum Rühren von Stahl in einer Pfanne durch dessen Rühren mittels elektromagnetischer Kräfte (siehe, z.B., "Injektionsmetallurgie", Übersetzung aus dem Englischen, herausgegeben von Sidorenko M.B., Moskau, "Metallurgie", 1986, S. 90).Also known is a method of stirring steel in a pan its stirring by means of electromagnetic forces (see, e.g. "Injection Metallurgy", edited by Sidorenko M.B., Moscow, "Metallurgy", 1986, p. 90).
Der Hauptnachteil dieses Verfahrens sind die hohen Kosten der eingesetzten Ausrüstung bei einem relativ niedrigen Rühreffekt.The main drawback of this process is the high cost of used equipment with a relatively low stirring effect.
Weiterhin bekannt ist ein Verfahren zum Rühren von Stahl in einer Pfanne, umfassend das Durchblasen des Stahls von unten mittels eines Gases oder Gas-Pulver-Gemisches durch im unteren Teil des Schmelzbades angeordnete Blasvorrichtungen, von denen mindestens eine aus der Pfannenmitte versetzt ist (s., z.B., die angegebene Quelle "Injektionsmetallurgie", S. 142 - 143 und Abb. 12). Obwohl bei der Durchführung des bekannten Verfahrens die Zufuhr des Gases oder Gas-Pulver-Gemisches durch spezielle Stopfen im Pfannenboden bevorzugt wird, schließt seine Durchführung die Zufuhr der angegebenen Komponenten durch eine eingetauchte Blasdüse (Blasdüsen) nicht aus.Also known is a method for stirring steel in a pan, comprising blowing the steel from below by means of a gas or gas-powder mixture through arranged in the lower part of the molten bath Blowing devices, of which at least one is offset from the middle of the pan (See, for example, the indicated source "Injection Metallurgy", pp. 142-143 and Fig. 12). Although in the practice of the known method, the supply of Gas or gas-powder mixture through special plugs in the bottom of the pan is preferred, its implementation concludes the supply of the specified Components by a submerged tuyere (tuyeres) is not enough.
Dieses bekannte Verfahren zum Rühren von Metall in einer Pfanne durch die Zufuhr von Gas oder eines Gas-Pulver-Gemisches kommt den wesentlichen Merkmalen nach dem erfindungsgemäßen Verfahren am nächsten und wird deswegen als nächstliegender Stand der Technik angenommen.This known method for stirring metal in a pan by the supply of gas or a gas-powder mixture comes the essential Characteristics closest to the method according to the invention and will therefore accepted as the closest prior art.
Dem bekannten Verfahren ist ein wesentlicher Nachteil eigen: im Laufe des Durchblasens des Stahls mittels des Gases/Gas-Pulver-Gemisches wird das Metall über das Pfannenvolumen ungleichmäßig gerührt. Vor allem die im Eintrittsweg des Gases/Gas-Pulver-Gemisches in den Stahl befindlichen Bereiche (aktivste Zone) des flüssigen Metalls werden einer intensiven Rührbewegung unterzogen. Bei der Annäherung des Gases/Gas-Pulver-Gemisches an die Oberfläche des Metalls in der Pfanne verbreitern sich diese Bereiche, durchströmen (unter Verringerung der Geschwindigkeit) die oberen Schichten des Schmelzbades und sinken von der Oberfläche als abgeschwächte absteigende Ströme herab. Selbstverständlich verringert dieses geschilderte Bild der Bewegung des gerührten Metalls die Effektivität des Rührens des Stahls, weil es das gesamte Metallvolumen in der Pfanne und insbesondere die Bodenzonen des Schmelzbades sehr langsam erfasst. Insgesamt wird die gestellte Aufgabe der Beschleunigung der Homogenisierung der Metallzusammensetzung nicht erreicht. Der bekannte Prozess erfordert einen erhöhten Einsatz an Gas und insbesondere an Zeit, welche im aktuellen technologischen Fertigungsvorgang des Stahls im wesentlichen nicht ausreichend zur Verfügung steht.The known method has a significant disadvantage: in the course of Blowing the steel by means of the gas / gas powder mixture is the Metal stirred unevenly over the pan volume. Especially the im Entry path of the gas / gas powder mixture in the steel areas (most active zone) of the liquid metal become an intense stirring motion subjected. When approaching the gas / gas powder mixture to the Surface of the metal in the pan widen these areas, flow through (reducing speed) the upper layers of the Melting bath and sink from the surface as weakened descending Streams down. Of course, this portrayed image reduces that Movement of stirred metal efficiency of stirring of steel because it the entire volume of metal in the pan and especially the bottom zones of the Melting bath detected very slowly. Altogether the posed task of the Acceleration of the homogenization of the metal composition is not achieved. The known process requires increased use of gas and in particular in time, which in the current technological manufacturing process of steel in the essential is not sufficiently available.
Das erfindungsgemäße Verfahren zum Rühren von Metall in einer Pfanne weist die genannten Nachteile nicht auf. Bei diesem Verfahren ist die aktive Zone der Erfassung des Metallvolumens durch das Gas/Gas-Pulver-Gemisch wesentlich verbreitert. Dies führt zur Verringerung der Zeit zur Erreichung einer homogenisierten Metallzusammensetzung ohne Erhöhung der zugeführten Gasmenge, d.h. die technische Aufgabe der Intensivierung des Rührens von Stahl in einer Pfanne mittels Durchblasens eines Gases/Gas-Pulver-Gemisches wird gelöst.The inventive method for stirring metal in a pan does not have the mentioned disadvantages. In this method, the active zone the detection of the metal volume by the gas / gas powder mixture significantly widened. This leads to the reduction of the time to reach a homogenized metal composition without increasing the supplied Amount of gas, i. the technical task of intensifying the stirring of steel in a pan by blowing a gas / gas powder mixture solved.
Die genannten technischen Ergebnisse werden dadurch erreicht, dass im Verfahren zum Rühren von Stahl in einer Pfanne, umfassend das Durchblasen des Stahls von unten mittels eines Gases/Gas-Pulver-Gemisches durch mindestens zwei vorgesehene Blasvorrichtungen, die auf diametral entgegengesetzten Seiten der Pfanne angeordnet sind, wobei erfindungsgemäß das Durchblasen abwechselnd zuerst durch eine der Blasvorrichtungen, die auf einer Seite der Pfanne angeordnet ist, und danach durch die andere Blasvorrichtung, die sich auf der anderen Seite der Pfanne befindet, erfolgt. Dabei hält man in der Blasvorrichtung, durch die momentan nicht durchgeblasen wird, einen Druck, der das Einfließen von Metall in diese Vorrichtung ausschließt. Die Periode des Betriebswechsels zwischen den Blasvorrichtungen vergrößert man mit der Erhöhung der Stahlmasse in der Pfanne. Das Volumen des zugeführten Gases wird bei der Umschaltung der Zufuhr des Gases oder Gas-PulverGemisches von einer Blasvorrichtung auf die andere unverändert belassen.The technical results mentioned are achieved in that A method of stirring steel in a pan, comprising blowing of the steel from below by means of a gas / gas powder mixture through at least two provided blowing devices, which are diametrically are arranged opposite sides of the pan, according to the invention the blowing through alternately first by one of the blowing devices, the on one side of the pan, and then the other Blowing device, which is located on the other side of the pan, takes place. there one stops in the blowing device, which does not blow through at the moment, a pressure which precludes the inflow of metal into this device. The Period of the operation change between the blowing devices is increased with the increase in steel mass in the pan. The volume of the supplied Gas is at the switching of the supply of gas or gas-powder mixture from one blowing device to the other left unchanged.
Das erfindungsgemäße Verfahren zum Rühren von Metall in einer Pfanne mittels Durchblasens von Gas oder eines Gas-Pulver-Gemisches wird an Hand von schematischen Zeichnungen näher erläutert.The inventive method for stirring metal in a pan by blowing of gas or a gas-powder mixture is on hand explained in more detail of schematic drawings.
In Abb. 1 ist eine Pfanne mit Metall dargestellt, in der zwei Blasvorrichtungen als Stopfen im Pfannenboden vorgesehen sind. In Abb. 2 ist eine analoge Pfanne mit zwei Blasvorrichtungen in Form von Blasdüsen dargestellt. In Abb. 3 ist die Ansicht in Richtung des Pfeils A gem. Abb. 1 dargestellt. Abb. 4 zeigt die Ansicht in Richtung des Pfeils A gem. Abb. 2. Dabei weist die Pfanne mindestens zwei Blasvorrichtungen auf. In Fig. 1, a pan is shown with metal, in the two Blowing devices are provided as a plug in the pan bottom. In Fig. 2 is an analogue pan with two blowing devices in the form of tuyeres shown. In Fig. 3, the view in the direction of arrow A gem. Fig. 1 shown. Fig. 4 shows the view in the direction of arrow A gem. Fig. 2. Here the pan has at least two blowing devices.
Die Stahlgießpfanne 1 ist mit dem flüssigen Stahl 2 gefüllt. Im
Pfannenboden (Abb. 1) sind auf diametral entgegengesetzten Seiten der Pfanne 1
(Abb. 3) mindestens zwei Blasvorrichtungen 3 vorgesehen. Die Anzahl dieser
Vorrichtungen kann höher, muß aber gerade sein. In der Pfanne 1 können auf
diametral entgegengesetzten Seiten der Pfanne 1 angeordnete Blasformen 4
vorgesehen sein. Die Blasformenanzahl kann höher, muß aber gerade sein. Das
Gas oder Gas-Pulver-Gemisch 5 wird der Pfanne jeweils durch Stopfen im
Pfannenboden (Abb.1) oder Blasdüsen 4 (Abb. 2) zugeführt. Das Gas oder das
Gas-Pulver-Gemisch können der Pfanne getrennt zugeführt werden. In diesem
Fall vergrößert man die Anzahl der Vorrichtungen 3 (Blasformen 4) bis zur
nächstfolgenden geraden Zahl. In Abb. 1 - 4 sind die Hauptströme des Metalls,
die sich bei der Zufuhr des Gases oder Gas-Pulver-Gemisches auf einer Seite der
Pfanne ausbilden, mit dünnen Linien 6 dargestellt. Diejenigen Ströme, welche sich
bei der Umschaltung der Blasvorrichtungen ausbilden, sind mit den Punktlinien 7
dargestellt. Eine Erhöhung der Anzahl der Stopfen 1 (Blasdüsen 4) verändert nicht
das Wesen oder den erzielten Effekt des vorgeschlagenen Verfahrens, steigert
aber zusätzlich die Intensivierung des Rührens des Stahls, d.h. erhöht die
Effektivität (verkompliziert aber gleichzeitig die Konstruktion).The ladle 1 is filled with the
Das Verfahren zum Rühren von Stahl in einer Pfanne wird folgenderweise durchgeführt.The method of stirring steel in a pan is as follows carried out.
In die Pfanne 1 wird der Stahl 2 eingegossen. Die für die Dotierung,
Desulfurierung und Entphosphorung des Stahles notwendigen Elemente werden
durch bekannte Verfahren oder als Pulver durch die beschriebenen
Vorrichtungen 3 (oder 4), oder durch beide Verfahren gleichzeitig in den Stahl
eingeführt. In the pan 1, the
Die Zufuhr des Gases (Gas-Pulver-Gemisches) 5 durch den Stopfen 3 (die
Blasform 4), der sich zum Beispiel in Abb. 1 - 4 links befindet, wird eingeschaltet.
Man verwendet Inertgas, zum Beispiel Argon. Im Ergebnis bilden sich in der
Metallschmelze die Hauptströme aus, die durch die Linien 6 dargestellt sind. In
dieser Zeit wird im Stopfen 3 (in der Blasdüse 4) auf der gegenüberliegenden
Seite der Pfanne ein Gasdruck gehalten, der das Einfließen des Stahls in diesen
ausschließt. Nach einer bestimmten Zeit (Periode) wird die Richtung der
Hauptströme des Metalls im Pfannenbad durch Zufuhr des Gases (Gas-PulverGemisches)
5 durch den Stopfen 3 (Blasform 4), der auf der gegenüberliegenden
Seite der Pfanne angeordnet ist (in Abb. 1 - 4 rechts), in die entgegengesetzte
Richtung geändert. Die Hauptströme des Metalls im Schmelzbad beginnen sich so
zu bewegen, wie es durch die Punktlinie 7 in den Abb. 1 - 4 dargestellt ist. Durch
den periodischen Wechsel der Bewegungsrichtung der Metallströme 6 → 7 → 6
usw. wird der Rührvorgang des Metalls wesentlich intensiviert. Im Ergebnis wird
im Laufe einer kürzeren Zeit eine homogenisierte Stahlzusammensetzung in der
Pfanne erhalten, d.h. die gestellte Aufgabe wird gelöst.The supply of the gas (gas-powder mixture) 5 through the plug 3 (the
Blow mold 4), for example, in Fig. 1 - 4 left, is turned on.
One uses inert gas, for example argon. The result is formed in the
Melt the main currents, which are represented by the
Die Periode des Richtungswechsels der Zufuhr des Gases (Gas-PulverGemisches)
wird praktisch bestimmt. Jedoch wird die Periodizität des
angegebenen Wechsels mit der Erhöhung der Stahlmasse in der Pfanne erhöht,
weil nur in diesem Fall die Metallströme 6 und 7 die gewünschte Form haben
(gezeigt auf den Abb. 1 und 2) und der Richtungswechsel der Zufuhr des Gases
(Gas-Pulver-Gemisches) sich minimal auf ihre gegenseitige Dämpfung auswirkt.The period of change of direction of supply of gas (gas-powder mixture)
is practically determined. However, the periodicity of the
specified change with the increase of the steel mass in the pan,
because only in this case, the
Es existiert eine Periode des Richtungswechsels, die für die vorgegebenen Bedingungen des Betriebs der Pfanne optimal ist. Eine Verringerung der Dauer dieser Periode ist nicht empfohlen, weil sich Zonen unvollständiger Homogenisierung der Schmelze im Stahlvolumen bilden. Eine Erhöhung der Dauer dieser Periode ist zulässig und wird durch den allgemeinen technologischen Rhythmus der Stahlerzeugung bestimmt. There is a period of change of direction for the given ones Conditions of operation of the pan is optimal. A reduction in duration this period is not recommended because zones are more incomplete Homogenization of the melt in the steel volume form. An increase in the Duration of this period is permissible and is governed by the general technological The rhythm of steelmaking is determined.
Ein "kaltes Modell" einer Pfanne 1 hatte die auf der Abb. 1 gezeigten
Abmessungen. In die Pfanne wurde Leitungswasser 2 bis zur Höhe von 430 mm
eingefüllt. Die Pfanne wurde mit drei Platinelektroden ausgerüstet: eine im unteren
Teil der Pfanne (Abstand vom Wasserspiegel 370 mm), eine im mittleren Teil der
Pfanne (Abstand vom Wasserspiegel 220 mm) und eine im oberen Teil der Pfanne
(Abstand vom Wasserspiegel 60 mm), die vorab in den Bereichen Leitungswasser
- 0,1 Gew.%ige wäßrige KCl-Lösung geeicht wurden. Alle drei Elektroden waren
55 mm von der Innenwand des Pfannenmodells entfernt. Außerdem war eine
tragbare Elektrode vorgesehen, mit der zusätzlich die Homogenisierung der
Lösung in den Zentren des Pfannenmodells, im Bodenteil, an der
Wasseroberfläche, sowie in den Fugen des Bodens und der Wände der Pfanne
ausgewertet wurde.A "cold model" of a pan 1 had the one shown in Fig. 1
Dimensions. In the pan was
Es wurde ein 20%-iges KCI-Konzentrat zubereitet und in einem dünnen
Gummiballon auf den Boden des Pfannenmodells in den Bereich nahe der
Pfannenwand, der 90° von den Vorrichtungen 3 gelegen war, abgesenkt. Der
Ballon wurde zerschnitten. Dabei wurde durch das 20%-ige KCl-Konzentrat nach
seiner gleichmäßigen Verteilung über die Wassermasse eine Konzentration von
0, 1 % KCl im Wasser eingestellt, auf welche die Elektroden geeicht wurden. Die
Verwendung des Ballons hat eine minimale störende Einwirkung auf das
Wasserbad gewährleistet.A 20% KCI concentrate was prepared and in a thin
Rubber balloon on the bottom of the pan model in the area near the
Pan wall, which was located 90 ° from the
Das Gas (Luft) wurde durch die Vorrichtungen im Boden in einer Menge von 6 l/min zugeführt. Bei einer größeren Luftzufuhr wurde das Blasenbildungsregime des Durchblasens gestört.The gas (air) was absorbed by the devices in the soil in an amount supplied from 6 l / min. For a larger air supply was the Bubble-forming regime of blow-through disturbed.
Unter den angegebenen Bedingungen und dem Durchblasen von Luft durch
eine Vorrichtung 3 ohne Richtungswechsel wurde nach 84 Min. eine homogene
0,1 Gew. % KCI-Lösung im Wasser der Pfanne erhalten. Dabei war die Lösung an
allen zusätzlich gemessenen Stellen über die ganze Lösungsmasse praktisch
gleich.Under the specified conditions and blowing air through
a
Unter den in Beispiel 1 angegebenen Bedingungen wurde eine abwechselnde Luftzufuhr mit einer Periode von 30 Sek. durchgeführt. Bei dem Richtungswechsel wurde die Menge der zugeführten Luft bei 6 l/min. gehalten. Nach 35 min wurde im Pfannenmodell eine homogene Lösung mit der obigen Konzentration erhalten, d.h. die Rührzeit wurde 2,4-fach im Vergleich zum Beispiel 1 verringert.Under the conditions given in Example 1 was a alternating air supply with a period of 30 sec. performed. In which Change in direction was the amount of air supplied at 6 l / min. held. After 35 min, the pan model became a homogeneous solution with the above Receive concentration, i. the stirring time was 2.4 times compared to Example 1 reduced.
Unter den in den Beispielen 1 und 2 angegebenen Bedingungen wurde eine abwechselnde Luftzufuhr mit einer Periode von 20 Sek. durchgeführt. Nach 60 min. wurde in der Pfanne eine homogene Lösung mit der obigen Konzentration erhalten, d.h. die Rührzeit wurde 1,4-fach im Vergleich zum Beispiel 1 verringert. Am Ende des 60-minütigen Rührens wurden im Wasservolumen Zonen mit größeren und kleineren Konzentrationen als 0,1% KCI in Wasser festgestellt, die von den Hauptelektroden nicht registriert wurden.Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 20 sec. performed. To 60 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.4 times compared to Example 1. At the end of the 60-minute stirring, there were zones in the water volume larger and smaller concentrations than 0.1% KCl detected in water were not registered by the main electrodes.
Unter den in den Beispielen 1 und 2 angegebenen Bedingungen wurde eine abwechselnde Luftzufuhr mit einer Periode von 10 Sek. durchgeführt. Nach 84 - 87 min. wurde in der Pfanne eine homogene Lösung mit der obigen Konzentration erhalten, d.h. die Rührzeit wurde im Vergleich zum Beispiel 1 praktisch beibehalten. Am Ende des Rührens wurden im Wasservolumen Zonen mit größeren und kleineren Konzentrationen als 0, 1 % KCI in Wasser festgestellt, die von den Hauptelektroden nicht registriert wurden. Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 10 sec. performed. After 84 - 87 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time became practical in comparison with Example 1 maintained. At the end of the stirring were in the water volume zones with larger and smaller concentrations than 0, 1% KCl detected in water, the were not registered by the main electrodes.
Unter den in den Beispielen 1 und 2 angegebenen Bedingungen wurde eine abwechselnde Luftzufuhr mit einer Periode von 40 Sek. durchgeführt. Nach 55 min. wurde in der Pfanne eine homogene Lösung mit der obigen Konzentration erhalten, d.h. die Rührzeit wurde 1,5-fach im Vergleich zum Beispiel 1 verringert. Im Wasservolumen fehlten Zonen mit einer KCI-Konzentration, die sich von der Konzentration von 0,1 Gew.% KCl unterschied.Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 40 sec. performed. To 55 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.5 times compared to Example 1. The water volume lacked zones with a KCI concentration that differed from the Concentration of 0.1 wt.% KCl difference.
Unter den in den Beispielen 1 und 2 angegebenen Bedingungen wurde eine abwechselnde Luftzufuhr mit einer Periode von 50 Sek. durchgeführt. Nach 60 min. wurde in der Pfanne eine homogene Lösung mit der obigen Konzentration erhalten, d.h. die Rührzeit wurde 1,4-fach im Vergleich zum Beispiel 1 verringert. Im Wasservolumen fehlten Zonen mit einer KCI-Konzentration, die sich von der Konzentration von 0,1 Gew.% KCI unterschieden.Under the conditions given in Examples 1 and 2 was a alternating air supply with a period of 50 sec. performed. To 60 min. was in the pan a homogeneous solution with the above concentration obtained, i. the stirring time was reduced 1.4 times compared to Example 1. The water volume lacked zones with a KCI concentration that differed from the Concentration of 0.1 wt.% KCI distinguished.
Das erfindungsgemäße Verfahren zum Rühren von Stahl in einer Pfanne gestattet durch eine einfache Verfahrensführung eine wesentliche Intensivierung des Rührvorganges des Stahls (eine Verringerung der Zeit zur Durchführung) ohne eine Einbuße an Rührqualität.The inventive method for stirring steel in a pan allows a substantial intensification by a simple process management the stirring of the steel (a reduction in the time to carry out) without a loss of stirring quality.
Claims (3)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2002108332/02A RU2208054C1 (en) | 2002-04-03 | 2002-04-03 | Method for mixing steel in ladle |
RU2002108332 | 2002-04-03 | ||
PCT/RU2002/000400 WO2003083145A1 (en) | 2002-04-03 | 2002-08-29 | Method for feeling steel |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1541699A1 true EP1541699A1 (en) | 2005-06-15 |
EP1541699A4 EP1541699A4 (en) | 2005-09-21 |
EP1541699B1 EP1541699B1 (en) | 2009-01-21 |
Family
ID=28673171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02768214A Expired - Lifetime EP1541699B1 (en) | 2002-04-03 | 2002-08-29 | Method for stirring steel |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP1541699B1 (en) |
AT (1) | ATE421598T1 (en) |
AU (1) | AU2002332367A1 (en) |
DE (1) | DE50213248D1 (en) |
ES (1) | ES2321071T3 (en) |
RU (1) | RU2208054C1 (en) |
UA (1) | UA77545C2 (en) |
WO (1) | WO2003083145A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1750075A1 (en) * | 2005-08-05 | 2007-02-07 | Vesuvius Becker & Piscantor Grossalmeroder Schmelztiegelwerke GmbH & Co. KG | Crucible for the treatment of molten metal and process for the manufacture thereof |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2910651A1 (en) * | 2014-02-19 | 2015-08-26 | Siemens VAI Metals Technologies GmbH | Method for the circulation of a metal bath and furnace construction |
RU2653743C1 (en) * | 2017-03-20 | 2018-05-14 | Публичное акционерное общество "Северсталь" (ПАО "Северсталь") | Method of mixing steel in the metallurgical unit |
CN111822665B (en) * | 2020-07-25 | 2021-12-21 | 莱芜钢铁集团银山型钢有限公司 | Argon blowing control method and argon control device for continuous casting tundish breathable upper nozzle pocket block |
CN115475933B (en) * | 2022-10-13 | 2024-04-26 | 莱芜钢铁集团银山型钢有限公司 | Protection method for argon blowing sealing of water gap of slab continuous casting machine |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1492953A (en) * | 1974-08-14 | 1977-11-23 | Inland Steel Co | Leaded steel bar |
JPH06235018A (en) * | 1993-02-09 | 1994-08-23 | Kawasaki Steel Corp | Method for controlling bottom-blowing gas in ladle refining |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE786018A (en) * | 1971-07-09 | 1973-01-08 | Allegheny Ludlum Ind Inc | PROCESS FOR INJECTING A REACTIVE GAS IN A BATH OF MELTED METAL |
SU1024509A1 (en) * | 1981-12-23 | 1983-06-23 | Днепродзержинский Ордена Трудового Красного Знамени Индустриальный Институт Им.М.И.Арсеничева | Method for converting crude iron |
RU2023017C1 (en) * | 1992-03-11 | 1994-11-15 | Пак Юрий Алексеевич | Apparatus for desulfurizing melt slag |
RU2132394C1 (en) * | 1998-06-02 | 1999-06-27 | Открытое акционерное общество "Северсталь" | Method for melting steel in arc steel melting furnace |
CN1087034C (en) * | 1999-11-02 | 2002-07-03 | 北京科技大学 | Technology for desulfurizing molten steel in enclosed ladle by spraying powder |
-
2002
- 2002-04-03 RU RU2002108332/02A patent/RU2208054C1/en not_active IP Right Cessation
- 2002-08-29 WO PCT/RU2002/000400 patent/WO2003083145A1/en not_active Application Discontinuation
- 2002-08-29 AU AU2002332367A patent/AU2002332367A1/en not_active Abandoned
- 2002-08-29 AT AT02768214T patent/ATE421598T1/en active
- 2002-08-29 ES ES02768214T patent/ES2321071T3/en not_active Expired - Lifetime
- 2002-08-29 DE DE50213248T patent/DE50213248D1/en not_active Expired - Lifetime
- 2002-08-29 EP EP02768214A patent/EP1541699B1/en not_active Expired - Lifetime
- 2002-08-29 UA UA20041210939A patent/UA77545C2/en unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1492953A (en) * | 1974-08-14 | 1977-11-23 | Inland Steel Co | Leaded steel bar |
JPH06235018A (en) * | 1993-02-09 | 1994-08-23 | Kawasaki Steel Corp | Method for controlling bottom-blowing gas in ladle refining |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN Bd. 018, Nr. 615 (C-1277), 24. November 1994 (1994-11-24) & JP 06 235018 A (KAWASAKI STEEL CORP), 23. August 1994 (1994-08-23) * |
See also references of WO03083145A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1750075A1 (en) * | 2005-08-05 | 2007-02-07 | Vesuvius Becker & Piscantor Grossalmeroder Schmelztiegelwerke GmbH & Co. KG | Crucible for the treatment of molten metal and process for the manufacture thereof |
Also Published As
Publication number | Publication date |
---|---|
ATE421598T1 (en) | 2009-02-15 |
WO2003083145A1 (en) | 2003-10-09 |
EP1541699A4 (en) | 2005-09-21 |
EP1541699B1 (en) | 2009-01-21 |
ES2321071T3 (en) | 2009-06-02 |
AU2002332367A1 (en) | 2003-10-13 |
RU2208054C1 (en) | 2003-07-10 |
UA77545C2 (en) | 2006-12-15 |
DE50213248D1 (en) | 2009-03-12 |
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