CA1339703C - Method for cleaning molten metal - Google Patents
Method for cleaning molten metalInfo
- Publication number
- CA1339703C CA1339703C CA000614559A CA614559A CA1339703C CA 1339703 C CA1339703 C CA 1339703C CA 000614559 A CA000614559 A CA 000614559A CA 614559 A CA614559 A CA 614559A CA 1339703 C CA1339703 C CA 1339703C
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- CA
- Canada
- Prior art keywords
- molten metal
- gas
- pressure
- vessel
- torr
- 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 - Fee Related
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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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
- C22B1/04—Blast roasting
-
- 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
- C21C7/10—Handling in a vacuum
-
- 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
-
- 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
- C21C7/0081—Treating and handling under pressure
-
- 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
Abstract
A method for cleaning molten metal comprises the steps of keeping a pressure inside a vessel having molten metal therein at a pressure of Ps of atmospheric pressure or less, bubbling the molten metal in the vessel by gas soluble in the molten metal, a portion of said gas dissolving in the molten metal and the rest of the gas converting to gas bubbles, and reducing rapidly the pressure in the vessel to pressure PE, fine gas bubbles being produced in the molten metal in the vessel, nonmetallic inclusions being trapped by said fine gas bubbles and by gas bubbles produced by bubbling and rising to the surface of the molten metal, and gas dissolved in the molten metal being removed. Pressure Ps in the step of keeping a pressure and pressure PE in the step of reducing the pressure are pressures Ps and PE of atmosphere inside the vessel in a zone enclosed with Ps=760, PE=40, (Ps)1/2 - (PE)1/2 = 3 06 in two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr.
Description
133g7~~
METHOD FOR CLEANING MOLTEN METAL
Background of the Invention Field of the Invention The present invention relates to a method for cleaning molten metal, and more particularly to a method for obtaining clean molten metal by making nonmetallic inclusions rise to the surface of the molten metal and removing the nonmetallic inclusions from the molten metal.
Description of the Related Arts Since inclusions ( for example, alumina inclusions in molten steel ) being suspended in molten metal are a cause of producing defects of quality of products, various methods for decreasing or removing the inclusions in molten steel have been proposed.
Out of methods having been very often used as comparatively effective methods, there is pointed out a method for removing inclusions from molten metal, wherein molten metal is bubbled by blowing inert gas from the bottom of a vessel into the molten metal under atmospheric pressure, gas bubbles thus produced trap the inclusions in the molten metal and the inclusions are removed after the inclusions have risen to the surface of the molten metal.
In the case of manufacturing a high quality steel, there is a need for limiting the total amount of oxygen in 133~~~
molten steel to 15 ppm or less. There, however, occurs a problem such that molten metal cannot be cleaned to more than ordinary norms of cleanness by the use of the above mentioned method. Therefore, a new method for cleaning molten metal has been expected to be developed.
That is, there have been difficulties in the prior art bubbling method in that a bubbling zone was limited to a zone which widened from a gas blow opening of the bottom of a vessel upwardly in the form of " V " and it was difficult to bubble molten steel from the entire vessel due to a limit of a gas blowing method. Moreover, there have been problems such that, since sizes of produced bubbles were large, molten metal flows as if it went around the bubbles during rising of the bubbles, fine inclusions move together with a flow of the molten metal, avoiding those bubbles, and, in consequence, the fine inclusions were hard to be trapped by the bubbles.
To overcome the above-mentioned difficulties, the present inventors propose the following method:
In this method, molten metal under elevated pressure is bubbled by a gas soluble in the molten metal, inclusions being suspended in the molten metal are trapped by gas bubbles produced by bubbling and by fine gas bubbles produced by reducing the pressure on pressurized molten metal. After the inclusions have risen to the surface of the molten metal, said inclusions are removed. Ordinary inclusions are trapped by first bubbling. Said trapped inclusions rise to the surface of the molten steel. On the other hand, since pressurized molten metal is bubbled, a large amount of bubbling gas dissolves in the molten metal.
Thereafter, gas having dissolved in the molten metal appears as fine gas bubbles from the entire zone of the molten metal by rapidly reducing a pressure inside a vessel.
During the bubbling, the fine inclusions are trapped by the bubbles and rise to the surface of the molten metal with the bubbles.
The above-mentioned method is very effective in removal of the inclusions in the molten metal. However, since the molten metal is pressurized at the initial stage of a processing step, some portion of the bubbling gas having once dissolved in the molten metal appears as fine gas bubbles during the reduction of the pressure on the molten metal, but the rest of the gas remains dissolved in the molten metal. Accordingly, one more processing step for degassing the molten metal is required after the above-mentioned processing of the gas has been carried out.
Therefore, there have been problems in that degassing capacity and the number of processing steps had to be increased. In addition, a cost for equipment increased because of the use of a pressure vessel.
Summary of the Invention It is an object of the present invention to provide a method for cleaning molten metal under reduced pressure 133~703 wherein the above-mentioned bubbling method is improved, a pressure vessel is not used, and degassing of the molten metal is carried out in the same vessel as that of bubbling method.
To accomplish the said object, the present invention provides a method for cleaning molten metal comprising the steps of:
keeping a pressure inside a vessel having molten metal therein at a pressure of Ps of atmospheric pressure or less;
bubbling the molten metal in the vessel by gas soluble in the molten metal, a portion of said gas dissolving in the molten metal and the rest of said gas converting to gas bubbles; and reducing rapidly the pressure in the vessel to pressure PE, fine gas bubbles being produced in the molten metal in the vessel, nonmetallic inclusions being trapped by said fine gas bubbles and by gas bubbles produced by bubbling and rising to the surface of the molten metal, and gas dissolved in the molten metal being removed.
In the method of the present invention, the molten metal is not processed under elevated pressure as in the prior art method. The molten metal is processed under reduced pressure after the molten metal has been bubbled by blowing gas soluble in the molten metal at atmospheric pressure or less. Particularly, in this processing under reduced pressure, not only the fine gas bubbles are simply 1~
produced, but also said bubbling gas remaining dissolved in the molten metal is removed together with the fine gas bubbles.
The above objects and other objects and advantages of the present invention will become apparaent from the detailed description to follow, taken in connection with the appended drawings.
Brief Description of the Drawings Fig.1 is a graphical representation showing the relation between a pressure inside a vessel during bubbling of molten metal by blowing nitrogen gas into the molten metal and a pressure inside the vessel during degassing of the molten metal according to the present invention;
Fig.2 is a vertical sectional view illustrating a refining apparatus for a ladle which carries out VOD
processing according to the present invention;
Fig.3 is a vertical sectional view illustrating a refining apparatus for a ladle which carries out VAD
processing according to the present invention;
Figs. 4 and 5 are explanatory view of a gas tight vessel having a horizontal rotation axis capable of rotating according to the present invention;
Fig.6 is a graphical representation showing a change of the total amount of oxygen in the molten steel with the lapse of time according to the present invention;
Fig.7 is an explanatory view designating another 133~703 example of the present invention wherein the same apparatus as in Fig.4 is used.
Fig.8 is a graphical representation showing the total amount of oxygen in the molten steel in another example different from Fig.6; and Figs.9 and 10 are explanatory views designating a vessel of rectangular parallelepiped having a gate therein.
Description of the Preferred Embodiment Preferred Embodiment-1 Fig.1 shows a result of having studied the case when molten steel was used as molten metal and nitrogen as gas soluble in the molten steel. Namely, Fig.1 is a graphical representation designating preferable zones out of coordinates of pressure Ps of atmosphere inside a vessel, under which the molten metal is bubbled by blowing said gas into the molten metal, and of reduced pressure PE of atmosphere inside the vessel. Units of Ps and PE are Torr.
Zone B shown with oblique lines is a preferable zone. Zone A
shown with crossing lines is more preferable zone. The zone B is a zone where the inclusions decrease. However, since the content of nitrogen ~N ~ in the molten steel poses problems depending on steel species, a denitrification step is sometimes required after processing of the molten steel under reduced pressure.
In Fig.1, a boundary ~ between the zones A and B, namely, PE = 40 Torr is determined in such a manner as described below. The relation between the pressure PN
inside the gas tight vessel and the content of nitrogen (N) in the molten steel is determined by an equilibrium relation of the folIwing equation (1) in the case of ordinary steel:
~ N~ = 450 (PN)1/2 .... - -- ( 1 ) Units of ~N ~ and PN are ppm and atm, respectively.
The allowable iargest value of ~N ) is estimated at 100 ppm.
~N ~ ~ 100 is obtained. ( N ) ~ 100 is substituted for the equation (1) and the pressure unit is converted from atm to Torr. PN ~ 38 Torr is obtained. PE = 40 Torr is obtained by rounding PN ~ 38 Torr.
Line ~ passing the lower ends of the zone B is determined for the following reason:
The amount of nitrogen removed from the molten steel which was required for trapping the inclusions and making the inclusions rise to the surface of the molten steel needed to be 50 ppm or more by experience of the present inventors. The amount of removed nitrogen is the difference between ~N ~ s and ~N ~ E . (N ~ s is the initial content of nitrogen increased by bubbling the molten steel by blowing nitrogen into the molten steel. ~N ~ E is the final content of nitrogen decreased by degassing the molten steel under reduced pressure. That is to say, the line ~ is determined by the use of the following equation obtained by putting said equation (1) into ~N ~ s - ~N ~ E 2 50 and representing pressures in Torr:
tPS) (PE)1/2 = 3.06 (2) The intersection point where the line ~ crossed the line ~
was ( 40, 88 ) in coordinates ( PE. PS ), PE = 40 being substituted for the equation (2). Further, in the case PN
is less than 75 Torr in the equation (1), it takes much time to make an equilibrium state between the pressure PN and the content ~ N ~ and this is ineffective. Ps of less than 75 Torr is considered difficult to apply. As a result, the line ~ passing the lower ends of the zone A was determined by connecting the point ( 0, 75 ) with the point ( 40, ~8 ). More preferable zone A is two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr. The zone A is enclosed with Ps=760, PE=0 and point (40, 88) and (0, 75) represented with (PE, PS). The preferable zone B is two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE. The zone B. is enclosed with Ps=760, PE=40 and (PS)1/2 - (PE)1/2= 3.06 . Out of the zone B, a zone enclosed with Ps=760, PE=40, PE=400 and (Ps) 1/2 - (PE)1 2 = 3.06 is more preferable in the two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr. Further, a zone enclosed with Ps=760, PE=40, PE=200 and (PS)1/2 - (PE)1/2 = 3.06 is most desired.
133~70~ -Example-1 An example of the present invention will be described with specific reference to the appended drawings. Fig.2 is a vertical sectional view illustrating a refining apparatus for a ladle having been used for the example of the present invention. In the drawings, referential numeral 30 denotes a gas tight vessel. Ladle 32 of 50 ton capacity, into which molten steel 31 is charged, is put into the vessel. Cover 33 of the gas tight vessel 30 is arranged in a removable state.
Lance 3~ is fixed to the cover to be used for VOD ( Vacuum Oxygen Decarbonization ). Referential numeral 35 denotes an exhaust opening for making the gas tight vessel vacuum.
Referential numeral 36 denotes a porous plug for blowing gas into the molten steel, which is arranged at the bottom of the ladle.
50 t of molten steel charged into the ladle 32 was kept at 1660 ~C and at 300 Torr in said gas tight vessel. 6 Nm3 of N2 was blown into the molten steel from the bottom of the ladle 32 for 10 min. Then, cover 33 was changed for another cover 38 having three electrodes as shown in Fig.3 to carry out VAD ( vacuum arc degassing ). Pressure in the vessel was rapidly reduced to 1 Torr,a heat compensation being made for the molten steel by means of said electrodes 37, and the pressure of 1 Torr was kept for 20 min. At the same time, the molten steel was bubbled by Ar gas blown into the molten steel from the bottom of the ladle at 150 N Q /min. A black point shown in Fig.1 corresponds to the Example-1.
_g_ ~ .~
The content of the molten steel obtained by processing of the molten steel in said Example-1 will be shown in Table 1 (all values are by weight). Example-2 shown in this Table will be described later. Results obtained in the case of using the prior art pressure elevation and reduction method (Control-1) wherein molten steel was degassed under reduced pressure after the molten steel had been bubbled by N2 gas under elevated pressure of more than atmospheric pressure and an Ar gas bubbling method (Control-2) are shown as controls in Table 1. In the pressure elevation and reduction method, the pressure in the vessel was increased to 3 atm during blowing of N2 gas and then reduced to 100 Torr during reduction of the pressure. As for other conditions, the molten steel was processed under the same conditions as those of the example of the present invention. Ar gas, however, was not blown into the molten steel during pressure reduction.
In the Ar gas bubbling method, 50 t of molten steel was kept at 0.5 to 1 Torr in a vacuous ladle and bubbled by Ar gas blown into the molten steel from the bottom of the ladle at a rate of 150 NQ/min for 20 min.
Table 1 Time,(min) Sol A~ T. T.
after C % Si % Mn % P % S % (0) (N~
Pressure % ppm ppm Reduction 0 0.13 0.32 1.12 0.023 0.006 0.048 42 147 Example-1 0.13 0.31 1.12 0.023 0.006 0.047 8 38 0.13 0.31 1.12 0.023 0.006 0.047 7 31 0 0.14 0.33 1.14 0.021 0.005 0.049 42 147 Example-2 0.14 0.32 1.13 0.021 0.005 0.047 7 60 0.14 0.32 1.13 0.021 0.005 0.047 5 35 Control-1 0 0.13 0.33 1.13 0.020 0.005 0.050 41 632 Pressure Elevation 10 0.13 0.32 1.13 0.020 0.005 0.048 9 279and Reduction Method 20 0.13 0.32 1.13 0.020 0.005 0.047 9 162 Control-2 0 0.12 0.33 1.15 0.018 0.005 0.054 42 20 Ar Gas Bubbling 10 0.12 0.32 1.14 0.018 0.005 0.054 24 19 Method 0.12 0.31 1.15 0.018 0.005 0.052 18 18 In Table 1, when Example-1 is compared with Control-1 or Control-2 relative to the total amount of oxygen T.[0) and the total amount of nitrogen T.(N) in the molten steel 20 min later after the pressure reduction,T.(0) in Example-1 decreased and T.(N) greatly decreased in comparison with the pressure elevation and reduction method. In comparison with the Ar gas bubbling method, it is recognized that T.(0) decreased. In this case, the amount of nitrogen increased slightly by blowing nitrogen gas, but such T.(N) does not pose any specific problem except for specific cases.
Preferred Embodiment-2 ~ hen the molten steel is stirred by blowing inert gas into the molten steel under reduced pressure as in the Example-1, soluble gas is remarkably removed from the molten steel and the amount of nitrogen decreased to the extent enough to be able to be put to practical use inspite of bubbling of the soluble gas in comparison with Control-1 and Control-2 in Table 1. The soluble gas, however, is removed during the pressure reduction and, at the same time, the occurrence of fine gas bubbles is also decreased.
Accordingly, it is thought that the effect of rising and separation of nonmetallic inclusions decreases with the lapse of time. Therefore, it is intended in Example-2 to keep the effect of the rising and separation of the nonmetallic inclusions by blowing the soluble gas together with the inert gas during the pressure reduction.
Example-2 An example of the present invention will be described specifically. As in Example-1, a refining apparatus for a ladle as shown in Figs.2 and 3 was used. Soluble gas was blown into molten steel before a pressure reduction, 50 t of molten steel being kept at 1660~C and at 300 Torr. 6 Nm3 of N2 gas was blown from the bottom of the ladle as shown in Fig.2 into the molten steel by means of a porous plug for 10 min. Then, cover 33 was changed for cover 38. Heat compensation was made for the molten steel by the use of arc heat of electrodes. Pressure in the ladle was rapidly reduced to 1 Torr and the pressure of 1 Torr was kept for 20 min. The molten steel was bubbled by blowing Ar gas as inert gas together with N2 gas from the bottom of the ladle at a rate of 150 N~/min. Flow of N2 gas was decreased to zero in the last five minutes as shown in Table 2 so as to make the amount of soluble gas as small as possible.
133970~
Table 2 Time after Pressure Reduction 0 ~ 10 10 ~ 15 15 ~ 20 Amount of Gas Blown into Ar 100 30 150 Molten Steel N~/min The components of molten steel which were obtained as a result of having processed the molten steel in Example-2 will be shown in Table 1. When Example-2 is compared with Example-1 in this Table, it is recognized that T.(0) was decreased by blowing nitrogen into the molten steel under reduced pressure while T.(N) was increased slightly.
The soluble gas is removed by pressure reduction in Preferred Embodiment-1 and Preferred Embodiment-2. However, in case a depth of a molten metal bath is large, a static pressure in a bottom portion of the molten metal bath becomes large. In consequence, it becomes difficult to degass the molten steel by the use of only processing of molten steel under reduced pressure. Specifically, when the depth of the molten steel is 1.5 m or more, the above-mentioned tendency became remarkable. To degass the molten metal in the bottom portion of the molten metal bath of large depth, it is thought to turn a gas tight vessel having the molten metal therein upside down and to greatly stir said molten metal under reduced pressure. This example will be described according to Example-3 and Example-4 shown below with specific reference to Figs.4 to 8.
Example-3 Fig.4 shows an example of a gas tight vessel 1 being able to be turned upside down with horizontal rotaton axis in a central portion thereof. Said gas tight vessel 1 is made cylindrical by tightly jointing vessel la and vessel lb , each of which has a form of a ladle of 2 m in diameter and 3 m in height. Gas blow opening 11 is positioned on an end face of the vessel lb. Exhaust opening for exhausting an atmospheric gas from vessel 1 is arranged in joint portion 13 of the vessels la and lb.
In this example, molten steel was cleaned by the use of the gas tight vessel 1 constituted with the vessels la and lb as described above. 50 t of molten steel 31 was charged into the vessel lb. Another vessel la was tightly jointed to the vessel lb from above to form the vessel 1. Then, N~
gas was blown into the vessel 1 through the gas blow opening 11 at a rate of 100 N ~/min to bubble the molten steel 31.
Gas was exhausted from the vessel 1 through said gas exhaust opening 12 so that the pressure inside the gas tight vessel 1 could not exceed a predetermined pressure. 20 minutes later, bubbling was stopped. In the above-mentioned state, the inside of the gas tight vessel 1 was made vacuous through said exhaust opening 12 with the use of a vacuum pump ( not shown ) so that the pressure inside the vessel 1 could be reduced to lo-2 Torr. When this degree of vacuum was kept,N2 having dissolved in the molten steel 31 appeared as fine gas bubbles which trapped fine inclusions in the molten steel 31 and made the fine inclusions rise to the surface of the molten steel.
minutes later after this, the gas tight vessel was turned counterclockwise at 180 ~ as shown in Fig.5 and was made to be in the upsidedown state as shown in Fig.4. Since a portion of the molten steel bath which had been in a deep position and had been under large static pressure was changed for a portion of molten steel bath of small depth, a static pressure decreased rapidly and a large amount of fine gas bubbles were produced from the portion of the molten steel bath of small depth. After the molten steel had been left in this state for 5 minutes, the gas tight vessel was turned clockwise at 180~ to be again in the state of Fig.4. In this case, the molten steel 31 was again stirred. Moreover, since the portion of the molten steel bath of large depth was changed for the portion of the molten steel bath of small depth, pressure on the portion of the molten steel bath having been under large static pressure was rapidly reduced, N2 gas having remained in the molten steel 31 appeared as fine gas bubbles. The molten steel was left in this state for 5 minutes. A vacuum pump was driven to keep the degree of vacuum at 10 -2 Torr during the pressure reduction.
Fig.6 shows a change of the total amount of oxygen in the molten steel 31 with the lapse of time in the example.
According to Fig.6, the total amount of oxygen in the molten steel could be decreased from initial ~0 ppm to final 12 ppm.
Example-4 An apparatus used for this method was the apparatus having been used in Example-3 as shown in Fig.4. As in Example-3, after molten steel had been kept in the gas tight vessel 1 and bubbled by blowing N2 gas into the molten steel through gas blow opening 11 positioned in the bottom of the vessel 1, pressure inside the gas tight vessel was reduced to 10-2 Torr by evacuating the gas tight vessel and the vacuum was kept. After the degree of vacuum had been kept for 5 min,the gas tight vessel 1 was turned at 90~ with central horizontal rotation axis 10 in a central portion thereof. The gas tight vessel 1 came to be in the state such that a longitudinal direction of the gas tight vessel of cylindrical shape was kept hori~ontally. Therefore, an area of bath of the molten steel 31 became large and a depth of the entire molten steel bath became small. As a result, a static pressure on a portion of the molten steel 31 which had been in a deep portion was reduced and fine gas bubbles began to be actively produced.
Fig.8 is a graphical representation designating a change of the total amount of oxygen T.(0) in the molten steel 31 which was processed by the above-mentioned degassing method wherein the depth of the molten steel bath was made small. As shown in Fig.8, it is understood that the degassing method is highly effective in processing of the molten steel since T.(0) in the molten steel was decreased from initial 80 ppm to final 15 ppm. In Example-3 wherein the gas tight vessel 1 was turned to 180~ , when rotation of the gas tight vessel 1 was stopped for a while at the position where the vessel was turned to 90 ~ , the effect of turning the gas tight vessel 1 at 180~ and 90 ~
can be obtained.
Example-5 Fig.9 is a schematic illustration showing another example of a method for promoting degassing of molten steel by making a depth of molten steel bath small. In this example, gas tight vessel 2 of parallelepiped of 3 m in width, 3 m in height and 8 m in length was used. Removable gate 3 of 3 m in length, 2.3 m in width and 0.5 m in thickness was arranged inside the gas tight vessel 2. The inside of the gas tight vessel 2 was divided into two chambers 2a and 2b. In the drawing, referential numeral 22 denotes an exhaust opening for exhausting inside atmosphere which is arranged in a ceiling of the gas tight vessel 2, 21 a gas injection opening arranged in the bottom of the chamber 2a, 23 an exit port for outflow of the molten steel which is arranged in the bottom of the chamber 2b and 24 an inlet for inflow of the molten steel which is arranged in a ceiling of the chamber 2a. Said gas injection opening 21 and said inlet for inflow of the molten steel are arranged so that they can be opened or closed if necessary.
A method for cleaning molten steel by the use of the gas tight vessel 2 constituted in such a manner as described above will be described. In Fig.9, gate 3 is positioned 2 m away from the left face of the gas tight vessel 2.
Approximately 90 t of molten steel 31 is charged through the inlet 24 for inflow of the molten steel into one chamber 2a separated from the other chamber 2b by the gate 3. During charging of the molten steel, the exit port 23 for outflow of the molten steel is closed. The volume of the molten steel 31 comes to be 12 m3 of 3 m in length, 2 m in width and 2 m in depth. N2 gas is blown through the gas blow opening 21 at a rate of 100 N Q /min and the molten steel 3 is bubbled by N2 gas. During bubbling, the inside atmosphere is simultaneously exhausted through said gas exhaust opening 22 so that there cannot be any excessive pressure inside the gas tight vessel. The bubbling of the molten steel is stopped 20 minutes later and the inside of the gas tight vessel 2 is evacuated through said gas exhaust opening 22 by the use of a vacuum pump ( not shown ). An opening is made between the bottom face and the lower ends of the gate 3 by lifting the gate 3 upwardly as shown in Fig.10 when the pressure inside the gas tight vessel 2 is reduced to 10-2 Torr. Then, the molten steel having been stemmed by said gate 3 spreads in the whole vessel 2. As a result, the depth of the molten steel 31 having been 2 m initially comes to be 0.5 m.
Since the depth of the molten steel becomes rapidly small and the area of the surface of the molten steel bath widens, fine gas bubbles are actively produced. ~hen the molten steel 31 is discharged by opening the exit port 23 for outflow of the molten steel, approximately the total amount of the molten steel flowed out of the vessel 2 a quarter of an hour later.
It is clearly understood that the above-mentioned method is highly effective in cleaning of molten steel since the total amount of oxygen was decreased from initial 80 ppm to final 12 ppm as a result of having cleaned the molten steel in such a manner as described above.
METHOD FOR CLEANING MOLTEN METAL
Background of the Invention Field of the Invention The present invention relates to a method for cleaning molten metal, and more particularly to a method for obtaining clean molten metal by making nonmetallic inclusions rise to the surface of the molten metal and removing the nonmetallic inclusions from the molten metal.
Description of the Related Arts Since inclusions ( for example, alumina inclusions in molten steel ) being suspended in molten metal are a cause of producing defects of quality of products, various methods for decreasing or removing the inclusions in molten steel have been proposed.
Out of methods having been very often used as comparatively effective methods, there is pointed out a method for removing inclusions from molten metal, wherein molten metal is bubbled by blowing inert gas from the bottom of a vessel into the molten metal under atmospheric pressure, gas bubbles thus produced trap the inclusions in the molten metal and the inclusions are removed after the inclusions have risen to the surface of the molten metal.
In the case of manufacturing a high quality steel, there is a need for limiting the total amount of oxygen in 133~~~
molten steel to 15 ppm or less. There, however, occurs a problem such that molten metal cannot be cleaned to more than ordinary norms of cleanness by the use of the above mentioned method. Therefore, a new method for cleaning molten metal has been expected to be developed.
That is, there have been difficulties in the prior art bubbling method in that a bubbling zone was limited to a zone which widened from a gas blow opening of the bottom of a vessel upwardly in the form of " V " and it was difficult to bubble molten steel from the entire vessel due to a limit of a gas blowing method. Moreover, there have been problems such that, since sizes of produced bubbles were large, molten metal flows as if it went around the bubbles during rising of the bubbles, fine inclusions move together with a flow of the molten metal, avoiding those bubbles, and, in consequence, the fine inclusions were hard to be trapped by the bubbles.
To overcome the above-mentioned difficulties, the present inventors propose the following method:
In this method, molten metal under elevated pressure is bubbled by a gas soluble in the molten metal, inclusions being suspended in the molten metal are trapped by gas bubbles produced by bubbling and by fine gas bubbles produced by reducing the pressure on pressurized molten metal. After the inclusions have risen to the surface of the molten metal, said inclusions are removed. Ordinary inclusions are trapped by first bubbling. Said trapped inclusions rise to the surface of the molten steel. On the other hand, since pressurized molten metal is bubbled, a large amount of bubbling gas dissolves in the molten metal.
Thereafter, gas having dissolved in the molten metal appears as fine gas bubbles from the entire zone of the molten metal by rapidly reducing a pressure inside a vessel.
During the bubbling, the fine inclusions are trapped by the bubbles and rise to the surface of the molten metal with the bubbles.
The above-mentioned method is very effective in removal of the inclusions in the molten metal. However, since the molten metal is pressurized at the initial stage of a processing step, some portion of the bubbling gas having once dissolved in the molten metal appears as fine gas bubbles during the reduction of the pressure on the molten metal, but the rest of the gas remains dissolved in the molten metal. Accordingly, one more processing step for degassing the molten metal is required after the above-mentioned processing of the gas has been carried out.
Therefore, there have been problems in that degassing capacity and the number of processing steps had to be increased. In addition, a cost for equipment increased because of the use of a pressure vessel.
Summary of the Invention It is an object of the present invention to provide a method for cleaning molten metal under reduced pressure 133~703 wherein the above-mentioned bubbling method is improved, a pressure vessel is not used, and degassing of the molten metal is carried out in the same vessel as that of bubbling method.
To accomplish the said object, the present invention provides a method for cleaning molten metal comprising the steps of:
keeping a pressure inside a vessel having molten metal therein at a pressure of Ps of atmospheric pressure or less;
bubbling the molten metal in the vessel by gas soluble in the molten metal, a portion of said gas dissolving in the molten metal and the rest of said gas converting to gas bubbles; and reducing rapidly the pressure in the vessel to pressure PE, fine gas bubbles being produced in the molten metal in the vessel, nonmetallic inclusions being trapped by said fine gas bubbles and by gas bubbles produced by bubbling and rising to the surface of the molten metal, and gas dissolved in the molten metal being removed.
In the method of the present invention, the molten metal is not processed under elevated pressure as in the prior art method. The molten metal is processed under reduced pressure after the molten metal has been bubbled by blowing gas soluble in the molten metal at atmospheric pressure or less. Particularly, in this processing under reduced pressure, not only the fine gas bubbles are simply 1~
produced, but also said bubbling gas remaining dissolved in the molten metal is removed together with the fine gas bubbles.
The above objects and other objects and advantages of the present invention will become apparaent from the detailed description to follow, taken in connection with the appended drawings.
Brief Description of the Drawings Fig.1 is a graphical representation showing the relation between a pressure inside a vessel during bubbling of molten metal by blowing nitrogen gas into the molten metal and a pressure inside the vessel during degassing of the molten metal according to the present invention;
Fig.2 is a vertical sectional view illustrating a refining apparatus for a ladle which carries out VOD
processing according to the present invention;
Fig.3 is a vertical sectional view illustrating a refining apparatus for a ladle which carries out VAD
processing according to the present invention;
Figs. 4 and 5 are explanatory view of a gas tight vessel having a horizontal rotation axis capable of rotating according to the present invention;
Fig.6 is a graphical representation showing a change of the total amount of oxygen in the molten steel with the lapse of time according to the present invention;
Fig.7 is an explanatory view designating another 133~703 example of the present invention wherein the same apparatus as in Fig.4 is used.
Fig.8 is a graphical representation showing the total amount of oxygen in the molten steel in another example different from Fig.6; and Figs.9 and 10 are explanatory views designating a vessel of rectangular parallelepiped having a gate therein.
Description of the Preferred Embodiment Preferred Embodiment-1 Fig.1 shows a result of having studied the case when molten steel was used as molten metal and nitrogen as gas soluble in the molten steel. Namely, Fig.1 is a graphical representation designating preferable zones out of coordinates of pressure Ps of atmosphere inside a vessel, under which the molten metal is bubbled by blowing said gas into the molten metal, and of reduced pressure PE of atmosphere inside the vessel. Units of Ps and PE are Torr.
Zone B shown with oblique lines is a preferable zone. Zone A
shown with crossing lines is more preferable zone. The zone B is a zone where the inclusions decrease. However, since the content of nitrogen ~N ~ in the molten steel poses problems depending on steel species, a denitrification step is sometimes required after processing of the molten steel under reduced pressure.
In Fig.1, a boundary ~ between the zones A and B, namely, PE = 40 Torr is determined in such a manner as described below. The relation between the pressure PN
inside the gas tight vessel and the content of nitrogen (N) in the molten steel is determined by an equilibrium relation of the folIwing equation (1) in the case of ordinary steel:
~ N~ = 450 (PN)1/2 .... - -- ( 1 ) Units of ~N ~ and PN are ppm and atm, respectively.
The allowable iargest value of ~N ) is estimated at 100 ppm.
~N ~ ~ 100 is obtained. ( N ) ~ 100 is substituted for the equation (1) and the pressure unit is converted from atm to Torr. PN ~ 38 Torr is obtained. PE = 40 Torr is obtained by rounding PN ~ 38 Torr.
Line ~ passing the lower ends of the zone B is determined for the following reason:
The amount of nitrogen removed from the molten steel which was required for trapping the inclusions and making the inclusions rise to the surface of the molten steel needed to be 50 ppm or more by experience of the present inventors. The amount of removed nitrogen is the difference between ~N ~ s and ~N ~ E . (N ~ s is the initial content of nitrogen increased by bubbling the molten steel by blowing nitrogen into the molten steel. ~N ~ E is the final content of nitrogen decreased by degassing the molten steel under reduced pressure. That is to say, the line ~ is determined by the use of the following equation obtained by putting said equation (1) into ~N ~ s - ~N ~ E 2 50 and representing pressures in Torr:
tPS) (PE)1/2 = 3.06 (2) The intersection point where the line ~ crossed the line ~
was ( 40, 88 ) in coordinates ( PE. PS ), PE = 40 being substituted for the equation (2). Further, in the case PN
is less than 75 Torr in the equation (1), it takes much time to make an equilibrium state between the pressure PN and the content ~ N ~ and this is ineffective. Ps of less than 75 Torr is considered difficult to apply. As a result, the line ~ passing the lower ends of the zone A was determined by connecting the point ( 0, 75 ) with the point ( 40, ~8 ). More preferable zone A is two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr. The zone A is enclosed with Ps=760, PE=0 and point (40, 88) and (0, 75) represented with (PE, PS). The preferable zone B is two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE. The zone B. is enclosed with Ps=760, PE=40 and (PS)1/2 - (PE)1/2= 3.06 . Out of the zone B, a zone enclosed with Ps=760, PE=40, PE=400 and (Ps) 1/2 - (PE)1 2 = 3.06 is more preferable in the two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr. Further, a zone enclosed with Ps=760, PE=40, PE=200 and (PS)1/2 - (PE)1/2 = 3.06 is most desired.
133~70~ -Example-1 An example of the present invention will be described with specific reference to the appended drawings. Fig.2 is a vertical sectional view illustrating a refining apparatus for a ladle having been used for the example of the present invention. In the drawings, referential numeral 30 denotes a gas tight vessel. Ladle 32 of 50 ton capacity, into which molten steel 31 is charged, is put into the vessel. Cover 33 of the gas tight vessel 30 is arranged in a removable state.
Lance 3~ is fixed to the cover to be used for VOD ( Vacuum Oxygen Decarbonization ). Referential numeral 35 denotes an exhaust opening for making the gas tight vessel vacuum.
Referential numeral 36 denotes a porous plug for blowing gas into the molten steel, which is arranged at the bottom of the ladle.
50 t of molten steel charged into the ladle 32 was kept at 1660 ~C and at 300 Torr in said gas tight vessel. 6 Nm3 of N2 was blown into the molten steel from the bottom of the ladle 32 for 10 min. Then, cover 33 was changed for another cover 38 having three electrodes as shown in Fig.3 to carry out VAD ( vacuum arc degassing ). Pressure in the vessel was rapidly reduced to 1 Torr,a heat compensation being made for the molten steel by means of said electrodes 37, and the pressure of 1 Torr was kept for 20 min. At the same time, the molten steel was bubbled by Ar gas blown into the molten steel from the bottom of the ladle at 150 N Q /min. A black point shown in Fig.1 corresponds to the Example-1.
_g_ ~ .~
The content of the molten steel obtained by processing of the molten steel in said Example-1 will be shown in Table 1 (all values are by weight). Example-2 shown in this Table will be described later. Results obtained in the case of using the prior art pressure elevation and reduction method (Control-1) wherein molten steel was degassed under reduced pressure after the molten steel had been bubbled by N2 gas under elevated pressure of more than atmospheric pressure and an Ar gas bubbling method (Control-2) are shown as controls in Table 1. In the pressure elevation and reduction method, the pressure in the vessel was increased to 3 atm during blowing of N2 gas and then reduced to 100 Torr during reduction of the pressure. As for other conditions, the molten steel was processed under the same conditions as those of the example of the present invention. Ar gas, however, was not blown into the molten steel during pressure reduction.
In the Ar gas bubbling method, 50 t of molten steel was kept at 0.5 to 1 Torr in a vacuous ladle and bubbled by Ar gas blown into the molten steel from the bottom of the ladle at a rate of 150 NQ/min for 20 min.
Table 1 Time,(min) Sol A~ T. T.
after C % Si % Mn % P % S % (0) (N~
Pressure % ppm ppm Reduction 0 0.13 0.32 1.12 0.023 0.006 0.048 42 147 Example-1 0.13 0.31 1.12 0.023 0.006 0.047 8 38 0.13 0.31 1.12 0.023 0.006 0.047 7 31 0 0.14 0.33 1.14 0.021 0.005 0.049 42 147 Example-2 0.14 0.32 1.13 0.021 0.005 0.047 7 60 0.14 0.32 1.13 0.021 0.005 0.047 5 35 Control-1 0 0.13 0.33 1.13 0.020 0.005 0.050 41 632 Pressure Elevation 10 0.13 0.32 1.13 0.020 0.005 0.048 9 279and Reduction Method 20 0.13 0.32 1.13 0.020 0.005 0.047 9 162 Control-2 0 0.12 0.33 1.15 0.018 0.005 0.054 42 20 Ar Gas Bubbling 10 0.12 0.32 1.14 0.018 0.005 0.054 24 19 Method 0.12 0.31 1.15 0.018 0.005 0.052 18 18 In Table 1, when Example-1 is compared with Control-1 or Control-2 relative to the total amount of oxygen T.[0) and the total amount of nitrogen T.(N) in the molten steel 20 min later after the pressure reduction,T.(0) in Example-1 decreased and T.(N) greatly decreased in comparison with the pressure elevation and reduction method. In comparison with the Ar gas bubbling method, it is recognized that T.(0) decreased. In this case, the amount of nitrogen increased slightly by blowing nitrogen gas, but such T.(N) does not pose any specific problem except for specific cases.
Preferred Embodiment-2 ~ hen the molten steel is stirred by blowing inert gas into the molten steel under reduced pressure as in the Example-1, soluble gas is remarkably removed from the molten steel and the amount of nitrogen decreased to the extent enough to be able to be put to practical use inspite of bubbling of the soluble gas in comparison with Control-1 and Control-2 in Table 1. The soluble gas, however, is removed during the pressure reduction and, at the same time, the occurrence of fine gas bubbles is also decreased.
Accordingly, it is thought that the effect of rising and separation of nonmetallic inclusions decreases with the lapse of time. Therefore, it is intended in Example-2 to keep the effect of the rising and separation of the nonmetallic inclusions by blowing the soluble gas together with the inert gas during the pressure reduction.
Example-2 An example of the present invention will be described specifically. As in Example-1, a refining apparatus for a ladle as shown in Figs.2 and 3 was used. Soluble gas was blown into molten steel before a pressure reduction, 50 t of molten steel being kept at 1660~C and at 300 Torr. 6 Nm3 of N2 gas was blown from the bottom of the ladle as shown in Fig.2 into the molten steel by means of a porous plug for 10 min. Then, cover 33 was changed for cover 38. Heat compensation was made for the molten steel by the use of arc heat of electrodes. Pressure in the ladle was rapidly reduced to 1 Torr and the pressure of 1 Torr was kept for 20 min. The molten steel was bubbled by blowing Ar gas as inert gas together with N2 gas from the bottom of the ladle at a rate of 150 N~/min. Flow of N2 gas was decreased to zero in the last five minutes as shown in Table 2 so as to make the amount of soluble gas as small as possible.
133970~
Table 2 Time after Pressure Reduction 0 ~ 10 10 ~ 15 15 ~ 20 Amount of Gas Blown into Ar 100 30 150 Molten Steel N~/min The components of molten steel which were obtained as a result of having processed the molten steel in Example-2 will be shown in Table 1. When Example-2 is compared with Example-1 in this Table, it is recognized that T.(0) was decreased by blowing nitrogen into the molten steel under reduced pressure while T.(N) was increased slightly.
The soluble gas is removed by pressure reduction in Preferred Embodiment-1 and Preferred Embodiment-2. However, in case a depth of a molten metal bath is large, a static pressure in a bottom portion of the molten metal bath becomes large. In consequence, it becomes difficult to degass the molten steel by the use of only processing of molten steel under reduced pressure. Specifically, when the depth of the molten steel is 1.5 m or more, the above-mentioned tendency became remarkable. To degass the molten metal in the bottom portion of the molten metal bath of large depth, it is thought to turn a gas tight vessel having the molten metal therein upside down and to greatly stir said molten metal under reduced pressure. This example will be described according to Example-3 and Example-4 shown below with specific reference to Figs.4 to 8.
Example-3 Fig.4 shows an example of a gas tight vessel 1 being able to be turned upside down with horizontal rotaton axis in a central portion thereof. Said gas tight vessel 1 is made cylindrical by tightly jointing vessel la and vessel lb , each of which has a form of a ladle of 2 m in diameter and 3 m in height. Gas blow opening 11 is positioned on an end face of the vessel lb. Exhaust opening for exhausting an atmospheric gas from vessel 1 is arranged in joint portion 13 of the vessels la and lb.
In this example, molten steel was cleaned by the use of the gas tight vessel 1 constituted with the vessels la and lb as described above. 50 t of molten steel 31 was charged into the vessel lb. Another vessel la was tightly jointed to the vessel lb from above to form the vessel 1. Then, N~
gas was blown into the vessel 1 through the gas blow opening 11 at a rate of 100 N ~/min to bubble the molten steel 31.
Gas was exhausted from the vessel 1 through said gas exhaust opening 12 so that the pressure inside the gas tight vessel 1 could not exceed a predetermined pressure. 20 minutes later, bubbling was stopped. In the above-mentioned state, the inside of the gas tight vessel 1 was made vacuous through said exhaust opening 12 with the use of a vacuum pump ( not shown ) so that the pressure inside the vessel 1 could be reduced to lo-2 Torr. When this degree of vacuum was kept,N2 having dissolved in the molten steel 31 appeared as fine gas bubbles which trapped fine inclusions in the molten steel 31 and made the fine inclusions rise to the surface of the molten steel.
minutes later after this, the gas tight vessel was turned counterclockwise at 180 ~ as shown in Fig.5 and was made to be in the upsidedown state as shown in Fig.4. Since a portion of the molten steel bath which had been in a deep position and had been under large static pressure was changed for a portion of molten steel bath of small depth, a static pressure decreased rapidly and a large amount of fine gas bubbles were produced from the portion of the molten steel bath of small depth. After the molten steel had been left in this state for 5 minutes, the gas tight vessel was turned clockwise at 180~ to be again in the state of Fig.4. In this case, the molten steel 31 was again stirred. Moreover, since the portion of the molten steel bath of large depth was changed for the portion of the molten steel bath of small depth, pressure on the portion of the molten steel bath having been under large static pressure was rapidly reduced, N2 gas having remained in the molten steel 31 appeared as fine gas bubbles. The molten steel was left in this state for 5 minutes. A vacuum pump was driven to keep the degree of vacuum at 10 -2 Torr during the pressure reduction.
Fig.6 shows a change of the total amount of oxygen in the molten steel 31 with the lapse of time in the example.
According to Fig.6, the total amount of oxygen in the molten steel could be decreased from initial ~0 ppm to final 12 ppm.
Example-4 An apparatus used for this method was the apparatus having been used in Example-3 as shown in Fig.4. As in Example-3, after molten steel had been kept in the gas tight vessel 1 and bubbled by blowing N2 gas into the molten steel through gas blow opening 11 positioned in the bottom of the vessel 1, pressure inside the gas tight vessel was reduced to 10-2 Torr by evacuating the gas tight vessel and the vacuum was kept. After the degree of vacuum had been kept for 5 min,the gas tight vessel 1 was turned at 90~ with central horizontal rotation axis 10 in a central portion thereof. The gas tight vessel 1 came to be in the state such that a longitudinal direction of the gas tight vessel of cylindrical shape was kept hori~ontally. Therefore, an area of bath of the molten steel 31 became large and a depth of the entire molten steel bath became small. As a result, a static pressure on a portion of the molten steel 31 which had been in a deep portion was reduced and fine gas bubbles began to be actively produced.
Fig.8 is a graphical representation designating a change of the total amount of oxygen T.(0) in the molten steel 31 which was processed by the above-mentioned degassing method wherein the depth of the molten steel bath was made small. As shown in Fig.8, it is understood that the degassing method is highly effective in processing of the molten steel since T.(0) in the molten steel was decreased from initial 80 ppm to final 15 ppm. In Example-3 wherein the gas tight vessel 1 was turned to 180~ , when rotation of the gas tight vessel 1 was stopped for a while at the position where the vessel was turned to 90 ~ , the effect of turning the gas tight vessel 1 at 180~ and 90 ~
can be obtained.
Example-5 Fig.9 is a schematic illustration showing another example of a method for promoting degassing of molten steel by making a depth of molten steel bath small. In this example, gas tight vessel 2 of parallelepiped of 3 m in width, 3 m in height and 8 m in length was used. Removable gate 3 of 3 m in length, 2.3 m in width and 0.5 m in thickness was arranged inside the gas tight vessel 2. The inside of the gas tight vessel 2 was divided into two chambers 2a and 2b. In the drawing, referential numeral 22 denotes an exhaust opening for exhausting inside atmosphere which is arranged in a ceiling of the gas tight vessel 2, 21 a gas injection opening arranged in the bottom of the chamber 2a, 23 an exit port for outflow of the molten steel which is arranged in the bottom of the chamber 2b and 24 an inlet for inflow of the molten steel which is arranged in a ceiling of the chamber 2a. Said gas injection opening 21 and said inlet for inflow of the molten steel are arranged so that they can be opened or closed if necessary.
A method for cleaning molten steel by the use of the gas tight vessel 2 constituted in such a manner as described above will be described. In Fig.9, gate 3 is positioned 2 m away from the left face of the gas tight vessel 2.
Approximately 90 t of molten steel 31 is charged through the inlet 24 for inflow of the molten steel into one chamber 2a separated from the other chamber 2b by the gate 3. During charging of the molten steel, the exit port 23 for outflow of the molten steel is closed. The volume of the molten steel 31 comes to be 12 m3 of 3 m in length, 2 m in width and 2 m in depth. N2 gas is blown through the gas blow opening 21 at a rate of 100 N Q /min and the molten steel 3 is bubbled by N2 gas. During bubbling, the inside atmosphere is simultaneously exhausted through said gas exhaust opening 22 so that there cannot be any excessive pressure inside the gas tight vessel. The bubbling of the molten steel is stopped 20 minutes later and the inside of the gas tight vessel 2 is evacuated through said gas exhaust opening 22 by the use of a vacuum pump ( not shown ). An opening is made between the bottom face and the lower ends of the gate 3 by lifting the gate 3 upwardly as shown in Fig.10 when the pressure inside the gas tight vessel 2 is reduced to 10-2 Torr. Then, the molten steel having been stemmed by said gate 3 spreads in the whole vessel 2. As a result, the depth of the molten steel 31 having been 2 m initially comes to be 0.5 m.
Since the depth of the molten steel becomes rapidly small and the area of the surface of the molten steel bath widens, fine gas bubbles are actively produced. ~hen the molten steel 31 is discharged by opening the exit port 23 for outflow of the molten steel, approximately the total amount of the molten steel flowed out of the vessel 2 a quarter of an hour later.
It is clearly understood that the above-mentioned method is highly effective in cleaning of molten steel since the total amount of oxygen was decreased from initial 80 ppm to final 12 ppm as a result of having cleaned the molten steel in such a manner as described above.
Claims (10)
1. A method for cleaning molten metal comprising the steps of:
keeping a pressure inside a vessel having molten metal therein at a pressure of Ps of atmospheric pressure or less;
bubbling the molten metal in the vessel by gas soluble in the molten metal, a portion of said gas dissolving in the molten metal and the rest of said gas converting to gas bubbles;
after bubbling said gas through said molten metal for at least five minutes, producing in the molten metal in the vessel, by pressure reduction to a pressure PE in said vessel, gas bubbles of a smaller size than the bubbles into which said gas is converted by the bubbling step and thereby trapping nonmetallic inclusions by said smaller size gas bubbles and raising them to the surface of the molten metal;
stopping the bubbling of said gas, and continuing the maintenance of reduced pressure for at least five minutes after the end of bubbling and thereby removing gas dissolved in the molten metal.
keeping a pressure inside a vessel having molten metal therein at a pressure of Ps of atmospheric pressure or less;
bubbling the molten metal in the vessel by gas soluble in the molten metal, a portion of said gas dissolving in the molten metal and the rest of said gas converting to gas bubbles;
after bubbling said gas through said molten metal for at least five minutes, producing in the molten metal in the vessel, by pressure reduction to a pressure PE in said vessel, gas bubbles of a smaller size than the bubbles into which said gas is converted by the bubbling step and thereby trapping nonmetallic inclusions by said smaller size gas bubbles and raising them to the surface of the molten metal;
stopping the bubbling of said gas, and continuing the maintenance of reduced pressure for at least five minutes after the end of bubbling and thereby removing gas dissolved in the molten metal.
2. The method of claim 1, wherein said pressure Ps in the step of keeping a pressure and said pressure PE in the step of reducing the pressure are pressures Ps and PE of atmosphere inside the vessel in a zone enclosed with Ps=760, PE=40 and (Ps) 1/2 - (PE)1/2 = 3.06 in two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr.
3. The method of claim 2, wherein said pressure Ps and said pressure PE are pressures Ps and PE of atmosphere inside the vessel in a zone enclosed with Ps=760, PE=40, PE=400 and (Ps) 1/2 - (PE)1/2 = 3.06 in the two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr.
4. The method of claim 3, wherein said pressure Ps and said pressure PE are pressures Ps and PE of atmosphere inside the vessel in a zone enclosed with Ps=760, PE=40, PE=200 and (Ps) 1/2 - (PE)1/2 = 3.06 in the two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr.
5. The method of claim 1, wherein the pressure Ps in the step of keeping a pressure and the pressure PE in the step of reducing the pressure are pressures Ps and PE of atmosphere inside the vessel in a zone enclosed with Ps=760, PE=40, PE=0 and a line connecting points (40,88) and (0,75) represented with coordinates (PE, PS) in the two-dimensional rectangular coordinates, whose ordinate is Ps Torr and whose abscissa is PE Torr.
6. The method of claim 1, wherein said gas soluble in the molten metal in the step of bubbling is N2.
7. The method of claim 1, wherein said step of producing smaller size bubbles by pressure reduction includes stirring said molten metal by blowing inert gas into molten metal.
8. The method of claim 7, wherein said gas soluble in the molten metal is continued to be blown in the molten metal during the blowing of inert gas into the molten metal until not less than five minutes before the end of the blowing-in of said inert gas.
9. The method of claim 1, wherein bubbling is stopped before said pressure reduction and wherein said vessel is gas tight and turnable as a whole as well as connected for evacuation and for blowing gas in and wherein said step of producing smaller-size bubbles by pressure reduction is aided by turning said vessel having the molten metal therein in such a way that molten metal is caused to shift from a deep molten metal bath configuration favorable for bubbling over to a shallower metal bath configuration favorable for degassing.
10. The method of claim 1, wherein said vessel is gas-tight as well as connected for blowing gas in and for evacuation and has means for decreasing the bath depth of molten metal by permitting lateral extension of the molten metal bath within said vessel and wherein said step of producing smaller-size bubbles by pressure reduction is aided by decreasing said depth of the molten metal bath held in the gas tight vessel.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP250807/88 | 1988-10-06 | ||
| JP63250807A JPH0742524B2 (en) | 1988-10-06 | 1988-10-06 | Method for cleaning molten metal |
| JP25080688A JP2718096B2 (en) | 1988-10-06 | 1988-10-06 | Vacuum cleaning method for molten metal |
| JP250806/88 | 1988-10-06 | ||
| JP031105/89 | 1989-02-13 | ||
| JP1031105A JPH02211974A (en) | 1988-01-21 | 1989-02-13 | Method for purifying molten metal by reduction of pressure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1339703C true CA1339703C (en) | 1998-03-10 |
Family
ID=27287204
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000614559A Expired - Fee Related CA1339703C (en) | 1988-10-06 | 1989-09-29 | Method for cleaning molten metal |
Country Status (6)
| Country | Link |
|---|---|
| EP (1) | EP0362851B1 (en) |
| KR (1) | KR920006578B1 (en) |
| AU (2) | AU4245789A (en) |
| BR (1) | BR8905068A (en) |
| CA (1) | CA1339703C (en) |
| DE (1) | DE68905741T2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5004495A (en) * | 1990-02-05 | 1991-04-02 | Labate M D | Method for producing ultra clean steel |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1582780A (en) * | 1968-01-10 | 1969-10-10 | ||
| US3635696A (en) * | 1968-05-21 | 1972-01-18 | Finkl & Sons Co | Treatment of molten metal using arc heat and vacuum |
| DE2710577A1 (en) * | 1977-03-11 | 1978-09-14 | Thyssen Edelstahlwerke Ag | METHOD OF REFRESHING STEEL |
| DE3426736A1 (en) * | 1984-07-20 | 1986-01-30 | Klöckner CRA Technologie GmbH, 4100 Duisburg | METHOD FOR THE PURGE GAS TREATMENT OF METAL MELT |
| GB2162604B (en) * | 1984-07-30 | 1988-05-25 | Teves Gmbh Alfred | Braking pressure generator for a hydraulic brake system |
| US4780134A (en) * | 1986-09-23 | 1988-10-25 | A. Finkl & Sons Co. | Simplified method and apparatus for treating molten steel |
-
1989
- 1989-09-29 CA CA000614559A patent/CA1339703C/en not_active Expired - Fee Related
- 1989-10-02 AU AU42457/89A patent/AU4245789A/en not_active Abandoned
- 1989-10-05 DE DE8989118517T patent/DE68905741T2/en not_active Expired - Fee Related
- 1989-10-05 EP EP89118517A patent/EP0362851B1/en not_active Expired - Lifetime
- 1989-10-05 BR BR898905068A patent/BR8905068A/en not_active IP Right Cessation
- 1989-10-06 KR KR1019890014420A patent/KR920006578B1/en not_active IP Right Cessation
-
1992
- 1992-04-02 AU AU13976/92A patent/AU655245B2/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| AU4245789A (en) | 1990-08-16 |
| KR900006541A (en) | 1990-05-08 |
| EP0362851A3 (en) | 1990-06-20 |
| KR920006578B1 (en) | 1992-08-10 |
| AU1397692A (en) | 1992-05-28 |
| AU655245B2 (en) | 1994-12-08 |
| DE68905741D1 (en) | 1993-05-06 |
| EP0362851B1 (en) | 1993-03-31 |
| EP0362851A2 (en) | 1990-04-11 |
| BR8905068A (en) | 1990-05-08 |
| DE68905741T2 (en) | 1993-09-23 |
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