CA1266756A - Method of and apparatus for continuously casting metals - Google Patents

Abstract

METHOD OF AND APPARATUS FOR CONTINUOUSLY
CASTING METALS

ABSTRACT OF THE DISCLOSURE

Molten metal is continuously teemed from a ladle into a tundish. The latter feeds a continuous stream of the molten metal to a cooled mold having opposite open ends connected by a casting passage.
The molten metal enters the mold at one end and partially solidifies in the casting passage to form a continuously cast strand which is withdrawn from the mold at its other end. The strand initially consists of a thin shell of solidified metal, and a molten core which is confined by the shell. Upon leaving the mold, the strand is conveyed through a bath of molten metal. The metal of the bath has a lower melting point than, and a specific gravity comparable to that of, the metal being cast. The bath functions to cool the strand uniformly so that the quality of the strand is maintained. The bath further counteracts the tendency of the molten core to cause bulging of the solidified shell which also serves to enhance the quality of the strand. Additional enhancement of the quality of the strand is obtained by virtue of the fact that the bath protects the strand from the atmosphere. The strand leaves the bath after the molten core has solidified and is then cut into sections for further processing.

Description

~266756 ,_ , ,. -- 1 .

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BACKGR8UND OF THE INVENT~ON

The invention relates genlerally to continuous casting.
More particularly, the invention relates to the continuous casting of metals, especially steel.
In the continuous casting of steel, molten steel is tee~ed into one end of a mold havin~
opposite open ends, and a strand consisting of a solidified shell and a molten core is withdrawn from the other end of the mold. Upon exiting from the mold, the strand is sprayed with water, or a mixtuee of water and air, in order to solidify the molten core.
The great majority oE continuous casting machines currently in use have vertical molds, and the molten steel is teemed into the upper end of the mold while the continuously cast strand is withdrawn from the lower end of the mold. The strand follows a downward path which,~depending upon the type of machine, may be straight or curve towards the horizontal. In either event, significant pressure develops inside the strand when the cross section of the latter is large. This is due to the fact that the rate at which heat can be removed from a strand is limited so that, for a large strand, the core remains molten for a substantial distance from the mold. The pressure generated by the molten core, which may be referred to as the metallostatic pressure, is a function of the specific gravity of the steel being cast and the head of the molten steel, that is, the vertical distance from the mold.
In order to counteract the metallostatic pressure, continuous casting machines for lar~e strands have roller aprons which receive the strand as it issues from the mold. The roller aprons, which s~ ~

_ - 2 -1 consist of two series of rollers located on opposite sides of the strand, generally extend from the mold - to at least that point along the path of the strand where the molten core has solidified completely. The cooling medium i6 sprayed onto thle strand through the spaces between neighboring rollers. The roller aprons also perform a guiding function.
One of the drawbacks of conventional continuous casting machines for large strands resides in that the roller apron adds significantly to the cost and complexity of the machine. An important factoc in the cost and complexity of the roller apron is the requirement that lt be able to withstancl the 3ubst~ntial metallostatic pre5suce oE the molten }5 core. Furthermore, although the roller apron counteracts the metallostatic pressure at the points of contact between the rollers and the strand, the metallostatic pressure causes bulging of the strand in the spaces between neighboring rollers.
Accordingly, as the strand travels along the roller apron, the shell of the strand bulges outwards in the spaces between neighboring rollers and is subsequently pushed inwards by the rollers. The alternating stresses generated in this manner may lead to defects in the strand.
Conventional continuous casting machines, including machines for small strands, also have a host of drawbacks related to the spray cooling of the strand. One such drawback is that homogeneous ~ooling is very difficult to achieve.
Non-homogeneous cooling is another source of defects in continuously cast strands. Furthermore, non-homogeneous cooling results in distortion of the geometric shape of the strand.
Another drawback related to spray cooling is ,, 6~i7~i6 . _ - 3 -___ _ 1 that the spray nozzles tend to become clogged. This not only enhances non-homogeneous cooling of the strand but adds to maintenance costs.
Moreover, the surface of the stand oxidizes during spray cooling. The scaling which accompanies oxidation results in loss of material. Oxidation al50 adversely affects surface qua~ity so that a surface layer of the strand must be removed after casting when good surface quality is required, e.g.
19 when casting certain steel grades. This not only entails a further loss of material but increases labor c05ts as well. In addition, the scale ~enerated during spray cooling must be periodically removed ~rom the machine which again adds to maintenance costs.
Since the water used for spray cooling becomes contaminated, a water treatment system is necessary. Such a system not only constitutes a substantial capital expenditure but also represents a significant maintenance item.

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It is an object of the invention to provide a continuous casting method and apparatus which enable the pressure of a molten core to be counteracted more effectively than heretofore.
Another object of the invention is to provide a continuous casting method and apparatus which enable the expense associated with a roller apron to be reduced.
An additional object of the invention is to provide a continuous casting method and apparatus which enable more uniform cooling to be achieved.
A further object of the invention is to provide a continuous casting method and apparatus which enable the expenses associated with spray cooling to be reduced.
It is also an object of the inven~ion to provide a continuous casting method and apparatus which enable material 105s~s to be r~duced.
Yet another object of the invention is to provide a continuous casting method and apparatus which enable strand quality to be improved.
The preceding objects, as well as others which will become apparent as the description proceeds, are achieved by the invention.
According to the present invention there is provided a continuous casting apparatus comprising:
(a) a mold provided with a casting passage having an inlPt end for molten material, and an outlet end for a continuously cast strand of the material, said mold being designed for the continuous casting of steel;
(b) withdrawal means for withdrawing the strand from said mold and conveying the strand along a predetermined path; and (c) cooling means for cooling the strand downstream of said mold, said cooling means including container means, and a non-gaseous cooling substance in said .~

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container means surrounding and contacting at least a portion of said path, said substance being capable of adhering to the strand so as to form a coating on the latter, and said substance having a boiling point lower than the melting point of the strand to thereby permit removal of ! the coating by heating, said substance comprising zinc.
According to the present invention, there is also provided a continuous casting method comprising the steps of:
(a) continuously introducing molten material into one end of a casting passage having another end which is spaced from said one end;
(b) cooling said material in said passage to Eorm a continuously cast strand;
(c) ~ontinuously withdrawing said strand Erom sa:id passage via said other end;
(d) cooling said strand subs~quent to withdrawal from said passage by immersing said strand in a bath, said bath including a substance capable of adhering to said strand; and (e) withdrawing said strand from said bath while said substance adheres thereto so that said substance forms a coating on said strand, said substance having a boiling point lower than the melting point of said strand to thereby permit removal of said coating by heating.
In the present invention, use is made of a bath consisting of a cooling substance which can form a coating on the strand, and has a boiling point lower than the melting point of the strand. This permits the coating to be subse~uently removed from the strand by heating to a temperature below the melting point of the strand.
According to the method and apparatus of the present invention, the strand is immersed in a bath subsequent to leaving the mold. Since the pressure of the ~`

- ~667S6 bath at least partly counteracts the pressure of the molten core, the structural reguirements for any guide means which may be disposed in the bath need not be as strict as those for the roller aprons of the prior art. The effect of the bath may be enhanced by making the bath of a substance having a specific gravity comparable to that of the material being cast~ Further enhancement of the effect of the bath is possible by arranging for the surface of the bath to be lo~ated near or at the level of the mold. Under such circumstances, bulging of the strand may be entirely !

or almost entirely suppressed by the bath alone.
Suppression of bulging by the bath and the accompanying reduction or elimination of stresses in the solidified shell permit improvements in quality to be obtained.
Cooling of the strand in a bath has the further advantage that the uniformity of cooling may be increased. Again, this leads to improvements in quality, including better conformance of the strand to the desired geometric shape. Appropriate selection of the thermal conductivity of the bath also enables cooling to proceed at a relatively rapid rate which, in turn, makes it possible to cast at a relatively high speed. Moreover, by designlng the bath so tha-t the temperature of the strand has been reduced to the proper level bo~ore th~ strand leavos th~ bakh, spray coo:L~Lng o~ th~ ~trarld may be ellm:Lnated. Th.L~
maJces it possible to dispense with a water treatment system, and further eli[ninates -the main-tenance problems and costs associated with spray cooling. In addition, suitable selection of the composition of the bath enables oxidation of the surface of the strand to be reduced so that improvemen-ts in surface quality may be obtained. Scaling of -the s-trand may also be reduced thereby reducing material losses and the frequency with which scale must be removed from the apparatus.
The novel features which are considered as characteristic of the invention are set forth in particular in the appended claims. The improved continuous casting apparatus itself, however, both as to its construction and its mode of operation, together with additional features and advantages thereof, will be best understood from a perusal of the following detailed description of certain specific embodiments with reference to the accompanying drawings.

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FIG. 1 is a schematic longitudinal sectional view of a continuous casting apparatus according to the invention FIG. 2 is a schematic transverse sectional . view of another continuous casting apparatus in : accordance with the invention;
. FIGS. 3a and 3b show different guide roller : arrangements for use in the apparatus of FIGS. 1 and

2;
FIGS. 4a and 4b illustrate dif~erent arrangements of guide skidæ for use in the apparatus of FIGS. 1 and 2;
FIG. 5 is a schematic longitudinal sectional view of an additional continuous cast.ing apparatus according to the invention;
~' FIG. 6 is a schematic longitudinal sectional view of a further continuous casting apparatus in accordance with the invention;
FIG. 7 is a schematic longitudinal sectional view of a different continuous casting apparatus : according to the invention;
FIG. 8 is a schematic longitudinal sectional view of yet another continuous casting apparatus in accordance with the invention;
FIG. 9 illustrates an arrangement of teeming vessels for use in the apparatus of F~G. 8;
FIG. 10 is a schematic longitudinal sectional view of still a further continuous casting apparatus according to the invention;
FIG. 11 is a schematic longitudinal sectional view of an additional continuous casting apparatus in accordance with the invention; and FIG. 12 is a sectional view in the direction of the arrows XII-XII of FIG. 11.
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DES_RIPTION OF l'HE PREFERP<ED EMBODIMENTS

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FIG. 1 illustrates a continuous casting apparatus of the vertical mold type. The apparatus of FIG. 1) which is assumed to be designed for the continuous casting of steel, incluldes a mold 1 having a casting passage la. The mola 1 is shown as being of the curved type, and the casting passage la is accordingly curved. However~ tbe mold 1 could just .as well be provided with a straight casting passage.
The casting passage la bas an inlet end lb through which molten steel is teemed into the mold 1, and an outlet end lc through which a continuously cast strand 2 is withdrawn from the mold 1. ~rhe mold 1, which is entirely conventional and may be in the form of a tube mold or plate mold, is cooled in a manner known per se~ A conventional oscillator 3 is connected with the mold 1 and functions to reciprocate the latter during casting. The mold 1 is mounted on a non-illustrated casting platform in a manner known per se.
A tank 4 is disposed below the mold 1. The tank 4 is situated and designed in such a manner that a portion of the path A ~ollowed by the strand 2 after exiting the mold 1 is located in the tank 4.
The tank 4 is filled with a substance 5 which serves to cool the strand 2 once the latter has left the mold 1. Preferably, the height of the tank 4 is such that the upper end of the tank 4 is at a level above the outlet end lc of the mold 1. This makes it possible for the upper surface 6 of the substance S
to be situated at or slightly above the outlet end lc as shown.
Guide rollers 7a and 7b for guiding the strand 2 are disposed downstream of the mold 1 in the tank 4. The guide rollers 7a are located adjacent to ~2~67~ , ~.... ..

.. . . .. ..
- ~ 1 that ~ur face of the strand 2 which forms at the inner radius of the casting passage la while the guide rollers 7b are located adjacent to that surface of the strand 2 which forms at the outer radius of the casting passage la. Certain ones of the guide rollers 7a,7b cooperate to define a straightening section 7c which eliminates the curvature imparted ~o the strand 2 during formation of the latter in the curved casting passage la.
10 - The guide rollers 7b continue beyond the straightening section 7c. The guide rollers 7a, on the other hand, are replaced by skids 8 downstream of the straightening section 7c.
The strand 2 leaves the tank 4 at an end 4a thereof remote from the mold l. A scraping device 9 may be lQcated at the discharge end 4a of the tank 4 in order to remove the substance 5 from the surfaces of the strand 2 and/or to form a relatively smooth coating of the substance 5 on the strand 2.
A conventional, reversible withdrawal unit 10 is mounted outside of the tank 4 downstream of the discharge end 4a. The withdrawal unit 10 serves to feed a non-illustrated dummy bar, which is known per se, into the mold 1 prior to casting, and further serves to convey the strand 2 along the path A.
A torch unit ll, which is likewise conventional, is disposed downstream of the withdrawal unit 10. The torch unit 11 functions to subdivide the strand 2 into sections~
The substance 5 may be solid at room temperature. In such an event, it is necessary to melt the substance 5 before proceeding with a cast.
To this end, the tank 4 may accommodate a series of units 12 each of which includes a heating element.
; 35 Any type of heating element capable of melting the ~Z~i67~
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, -- 11 --_ . , -- 1 substance 5 may be used. For example, the heating - elements may be in the form of electrical resi~tance elements. Each of the units 12 may further include a pump for circulating the substance 5 subsequent to melting.
The heatin~ elements need not be formed 35 units 12 with the circulating pumps, and it is possible for the heating elements to be separate from the circulating pumps.
In order to recover the heat removed from the strand 2, one or more heat exchangers 13 may be disposed in the tank 4. Circulation of an appropriate cooling medium, e.g. water, through th~
heat exchangers 13 during casting then permits at least part of the heat transferred from the strand 2 to the substance 5 to be recovered.
When the tank 4 is provided with heat exchangers 13 for the purpose of recovering the heat removed from the strand 2, it is desirable to reduce heat losses from the tank 4. This may be accomplished by surrounding the tank 4 with insulation 14.
The tank 4 is illustrated as being open at the top. Howeverl it is entirely possible to enclose the substance 5 entirely by designing the tank 4 with a cover. A cover will reduce heat lossès from the tank 4 and may also function to suppress the escape of fumes into the atmosphere should this be a problem.
The continuous casting apparatus of FIG~ 1

3~ operates as follows:
It is assumed that the substance 5 is a solid at room temperature and is initially in solid form. Heat is supplied to the heating elements of the heating and ci~culating units 12 in order to melt the substance 5. Once the substance 5 has melted so ;G

as to form a bath, the circulating pumps of the heating and circulating units 12 may be started.
A non-illustrated, conventional dummy bar is now fed towards the mold 1 by the withdrawal unit 10. The dummy bar is positioned so that the dummy bar head closes the outlet end lc of the mold 1. The portion of the dummy bar remote from the dummy bar head remains engaged by the withdrawal unit 10.
A tundish 15 known per se is positioned above the mold 1. Once the dummy bar and the tundish 15 are in position and the dummy bar head has been sealed, a ladle 16 containing molten steel is transported to a location above the tundish 15 by a service crane 17. The ladle 16 is opened while th~ tun~i~h 15 remain~ ~alcd, and molt~n steel lS i8 t~m~d ~om ~h~ l~d.~ 16 into the ~undish lS ul~til th~
latter has bcen ~ d to a pr~determined leve:L. I'he tundish 15 is now opened, and the molten steel is -teemed from the tundish 15 into the inlet end lb of the mold 1.
The oscillator 3 is started and reciprocates the mold 1.
Furthermore, cooling of the mold 1 is initiated.
When the molten steel in the mold 1 reaches a specified level, the withdrawal unit 10 is started in order to draw the dummy bar away from the mold 1. The initial quantity of molten steel to enter the mold 1, which constitutes the leading end of the strand 2, solidifies upon contact with the dummy bar head and forms a connection with the latter.
Accordingly, the strand 2 is drawn out of the outlet end lc of the mold 1 as the dummy bar is pulled away from the mold 1 by the withdrawal unit 10. Since the upper surface 6 of the bath formed by the substance 5 is at or above the level of the outlet end lc, the strand 2 travels from the mold 1 directly into the bath. The strand 2 is thus prevented from coming into contact with the air at such ;7~6 time as the strand 2 is at its highest temperature which helps reduce oxidation of the strand 2.
Sufficient heat to maintain the substance 5 in liquid form is supplied by the heating elements of the heating and circulating units 12 during the interval between melting of the substance 5 and entry of the strand 2 into the bath formed by the substance 5. Circulation of a cooling medium through the heat exchangers 13 is avoided during this in-terval. When the strand 2 enters the bath, the heat output of the heating elements may be reduced inasmuch as large quantities of heat are now transferred to the bath from the initially white-hot strand 2.
Furthermore, circulation of a cooling medium through the heat exchangers 13 is begun upon entry of the strand 2 into the bath. Il~a~ ~ransmi~ted ~r~m the strand 2 in~o ~he bath is trans~erred ~o ~he coollng medium in the heat exchangers 13 by indirect heat exchange between the cooling medium and the bath. The cooling medium circulated through the heat exchangers 13 may be water, for example, and the heat recovered from the strand 2 may then serve to generate part or all of the hot water supply for the continuous casting facility.
As mentioned previously, the mold 1 is cooled in a conventional manner. Generally, the mold 1 will be cooled by circulating cool water through the same. Cooling of the mold 1 causes a thin layer of the molten steel~ adjacent to the walls of the casting passage la to solidi~y. This results in formation of the strand 2 which, when it first exits from the mold 1, consists of a very thin outer skin or solidified shell surrounding a molten core. Ih , C ~LZ6~

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1 upper surface or meniscus of ~he molten core is located in the mold 1 and remains in this position while the contents of the ladle 16 are emptied into the mola 1. The molten core-exerts a pressure on the solidified shell which is proportiomal to the vertical distance from the meniscus and tends to cause bulging of the solidified shell. ~owever, in accordance with the invention, bulging of the solidified shell is resisted by the bath of the 10 substance 5 which generates a pressure counteracting the pressure of the molten core~ The effectiveness o~ the bath in counteracting the outward pressure o~
the molten core is enhanced by having the upper surface 6 of the bath located at the level of the 15 mold 1. The reason is that the head of the bath at any point of the portion of the path A within the tank 4 is then almost the same as the head of the molten core at such point. The effectiveness of the bath in counteracting the outward pressure of the 20 ~olten core may be further enhanced by selecting the substance 5 so that the specific gravity of the bath equals or approximates the specific gravity of the molten core.
As the strand 2 travels downwards, the 25 metallostatic pressure due to the molten core increases since the head of the molten core increases. However, the pressure exerted by the bath likewise increases inasmuch as the depth to which the strand 2 is immersed in the bath, and hence the head 30 of the bath, increases with downward movement of the strand 2.
Cooling of the strand 2 by the bath causes the thickness of the solidified shell to increase progressively as the strand 2 travels along the path 35 A. Accordingly, the solidified shell becomes more , . .

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~ ~ 1 and more capable of containing the molten core on its own. This effect is enhanced by the fact that the solidified shell becomes progressively cooler as the strand 2 advances so that the strength of the s~lidified shell also increases progressively. The increase in thickness of the solidified shell is ; accompanied by shrinking of the molten core.
Since the casting passage la is curved, the strand 2 is formed with an inherent curvature and lo tends to follow a curved path having a radius eyual to that of the casting passage la. The guide rollers 7a,7b located upstream of the straightening section 7c define a path segment which has a radius oE
curvatu~e equal to that o~ the casting passa~e la ~nd constitute~ a continuation of the latter. On the other hand, the guide rollers 7a,7b of the straightening section 7c define a path segment of continuously increasing radius as considered in downstream direction of the path A. Thus, when the 20 strand 2 enters the straightening section 7c, the strand 2 is unbent. The straightening section 7c is designed in such a manner that the strand 2 is essentially straight upon leaving the straightening section 7c. From the straightening section 7c, the 25 strand 2 is guided to the discharge end 4a of the tank 4 along an essentially linear path segment bounded by the guide rollers 7b and the skids 8. As the strand 2 exits from the tank 4, the surfaces of the strand 2 are scraped by the scraping device 9 in 30 order to remove residues of the substance 50 For a strand 2 of solid cross section, the casting speed or rate of advance of the strand 2; the length of the portion of the path A in ~he substance 5; the heat output of the heating elements 35 constituting part of the heating and circulating C '~2~

=
1 units 12; and the rate of circulation of a cooling medium through the heat exchangers 13 are preferably selected in such a manner that the strand 2 is solidified throughout before leaving the bath.
After passing through the ~discharge end 4a of the tank 4, the strand 2 enters the withdrawal unit 10. Once the strand 2 has been engaged by the withdrawal unit 10, the strand 2 may be disconnected from the dummy bar. This may be accomplished in any 10 conventional manner, e.g. by cutting the strand 2 immediately upstream of the dummy bar head using the torch unit 11~ The strand 2 advances from the withdrawal unit 10 to the torch unit 11 where the strand 2 is cut into sections of predetermined length 15 in a manner known per se. Th~ cut sections are transported away from the torch unit 11 on a non-illustrated conveyor, e.g. a roller conveyor, for further processing as desired.
As described previously, one advantage of 20 the bath of the substance 5 is the resistance offered to the metallostatic pressure of the molten core.
Since the bath at least partially compensates for the metallostatic pressure, it follows that the guide rollers 7a,7b and the skids 8 are less highly 25 stressed than the roller aprons of the prior art which must bear the full effect of the metallostatic pressure. Furthermore, the buoyancy of t~e bath at least partly counteracts the weight of the strand 2 which further contributes to a reduction of the 30 stresses imposed upon the guide rollers 7b.
Accordingly, the guid~ means including the guide rollers 7a,7b and the skids 8 may be manufactured a~
a lower cost than the roller aprons of the prior art.
From a metallurgical point of view, there 35 may be benefits to be realized when the height of the ~ ~2~6~
,....

_ _ - 17 -~ _ .
1 molten core ~s great. In conventional continuous casting apparatus, great height of the molten core can be obtained only at high cost due o the strength requirements which are imposed on the roller apron by the large head ~ molten metal. The invention, on ~he other hand, makes it possible t:o achieve great height of the molten core relatively inexpensively.
The resistance of the bath to the metallostatic pressure of the molten core also 10 reduces the bulging which a strand undergoes between neighbor ing rollers of a conventional roller apron~
the reduction in bulging is accompanied by a decrease in the stresses and strains to which the solidified shell is subjected. As a result, improvements in 15 ~uality may be obtained. For example, interna} and external cracking of the strand 2 may be reduced.
The improvements in quality may be enhanced by arranging the upper surface 6 of the bath to be at the level of the mold 1 and by selecting the specific 20 gravity of the bath so that it is comparable to the specific gravity of the molten core. Under such circumstances, bulging of the strand 2 and defects associated with bulging may be virtually eliminated.
In conventional continuous casting 25 apparatus, breakouts occur in a certain percentage of the strands. In other words, the metallostatic pressure and the resultant bulging cause the solidified shell of a certain percentage of the strands to rupture. This percentage may also be 30 reduced in accordance with the invention.
A further advantage of the bath of the substance 5 is that it promotes uniform cooling of the strand 2. In the continuous casting apparatus of the prior art, the strand is sprayed with water, or a 35 mixture of air and water, by means of spray nozzles.

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~ :1 Generally, certain areas of the strand are oversprayed while others are undersprayed. This sets up thermal stresses in the strand which, in turn, lead to defects. The situation is aggravated when a spray nozzle becomes clogged durinlg a cast since safety considerations prevent accelss to the spray nozzles while casting is being performed. The bath of the invention makes it possible to reduce, or even virtually eliminate, thermal gradients caused by 10 non-uniform cooling. This enables additional improvements in quality to be obtained. Increased uniformity of cooling further helps to reduce distortion of the geometric shape of the strand 2.
The bath also per~it~ cooling o~ ~h~ strand lS 2 to be very accu~ately contr~lled. This may be accomplished by appropriate regulation of the heat exchangers 13 and/or the heating elements constituting part of the heating and circulating units 12 and/or the circulating pumps constituting 20 part of the units 12.
The bath of the substance 5 fur ther functions to protect the strand 2 from the atmosphere. As a result, scalin~ of the strand 2 may be reduced which, in turn, decreases material 25 losses. Moreover, inasmuch as reduced scaling of the strand 2 is accompanied by a reduction in the amount of debris deposited in the continuous casting apparatus, the costs associated with cleaning of the apparatus may be reduced. Improvements in the 30 surface quality of the strand 2 may also be achieved by virtue of the fact that the bath maintains the strand 2 out of contact with the atmosphere.
Protection of the strand 2 from the atmosphere ~ay be enhanced by arranging for the upper 35 surface 6 of the bath to be located at the level of ~Z667~ i _.
~_ -- 1 9 1 the mold 1 so that the outlet end lc of the latter is disposed in the bath. The strand 2 is then prevented from coming into contact with the iatmosphere when the strand 2 is at its highest temperature and ~ost s~sceptible to oxidation. The surface quality of the strand 2 upon emergence from the bath may then be as good as when the strand 2 exited the mold 1.
The surface of the strand 2 may continue to be protected from the atmosphere after leaving the 10 bath of the substance 5 if the latter is capable of forming a coating on the strand 2. The coating may be retained sho~lld this be necessary or desirable for further proce~sing. On the other hand, if proce~ssing consideration8 dictate that the ~trand 2 be uncoate-~, 15 the coating may be removed at any convenient time.
Preferably, removal of the coating is carried out after the cut sections of the strand 2 have been transported away from the continuous casting apparatus. The coating may be removed in any 20 conventional fashion. However, suitable selection of the substance 5 makes it possible to combine removal of the coating with another of the operations to which the cut sections of the strand 2 are subjected so that a separate operation for stripping the 25 coating may be avoided. For example, the cut sections of the strand 2 may be rolled. The rolling of steel sections is generally preceded by a heating operation at about 1100 C. If zinc is used as the substance S, the zinc coating which forms on the 3~ strand 2 may be evaporated durinq the preheating cycle since the boiling point of zinc is 907 C.
By appropriate selection of the rate of advance of the strand 2; the length of the portion of the path A in the bath of the substance S; the heat 35 output of the heating elements constituting part of lZ~
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-~~ 1 the heating and circulating units 12; and the rate of circulation of a cooling medium through the heat exchangers 13, the temperature of the strand 2 upon leaving the bath may be sufficiently low that further cooling of the strand 2 in the continuous casting apparatus is unnecessary. Spray cooling of the stran~ 2 may then be avoided entirely. This not only eliminates the costs involved in keeping the spray nozzles unplugged and properly aligned but also makes it possible to dispense with a water treatment system.
The bath additionally offers the possibility of recovering heat from the strand 2. No heat recovery can be achieved with the spray systems of the prior art.
In addition, selection of the substance S so that the thermal conductivity of the bath is relatively high permits a relatively high rate of heat transfer between the strand 2 and the bath to be achieved. The resulting rapid removal of heat from 20 the strand 2 makes it possible to achieve casting speeds higher than those which are obtainable for spray cooling.
The ernployment of a bath for cooling the strand 2 also opens a new avenue for the continuous 25 casting of hollow sections. In accordance with the invention, this may be accomplished by allowing the strand 2 to travel upwards to a point higher than the level of the meniscus, i.e. the level of the upper surface of the column of molten metal in the mold 1.
30 The casting speed or rate of advance of the strand 2;
the length of the portion of the path A in the bath;
the heat output of the heating elements constituting part of the heat;ng and circulatin9 units 12; and the rate of circulation of a cooling medium through the 35 heat Pxchangers 13 are then selected in such a manner 2667~

_ _ 1 that the core of th~ strand 2 is still ~olten when the strand 2 reaches the leYel of the meniscus.
Under such circumstances, the portion of the strand 2 above the meniscus will be hollow.
The meth-od and apparatus of the invention have the further advantage that all required components are commercially available.
The substance 5 desirably has the following ; properties:
A. It should be non-flammable up to the melting point of the material being cast.
B. It should not undergo any type of reaction with the material being cast which adversely affects the properties o~ the ultimate products.
C. It should have a melting point which is so much lower than the melting point of the - material being cast that a rate of heat transfer sufficiently high for the desired production rate may be achieved.
D. It should be solid or liquid at room temperature.
E. It should have a thermal conductivity of such large magnitude in the liquid phase that a rate of heat transfer sufficiently high for the 25 desired production rate may be achieved.
In addition to these properties, the substance 5 preferably has a specific gravity in the liquid phase which is comparable to that of the molten material being cast. If the specific gravity 30 of the substance 5 is far less than that of the material being cast, the bath may be unable to contain the molten core of the strand 2. On the other hand, if the specific gravity of the substance 5 far exceeds the specific gravity of the material 35 being cast, the bath may compress the strand 2.
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l For the casting of materials such as steel having high melting points, it is preferred for the substance 5 to be in the form of a pure metal or alloy having a relatively low melting point.
5 Advantageously, the melting point of the substance 5 does not exceed about 500C for the casting of steel~ While it is possible to use material~ having higher melting points, the energy required to melt the substance 5 may become excessiveO Furthermore, 10 the temperature gradient between the strand 2 and the bath of the substance 5 may be~ome too small for efficient cooling of the strand 2 if the melting point of the substance 5 is too high~ _ The specific grav~ty o the substance 5 at 15 room tempecature m~y lie in the ran~e of about 1 to 10 for the casting of steel. Preferably, however, the specific gravity of the substance 5 at room temperature is in the range of about 5 to B since the effectiveness of the bath in counteracting the 20 metallostatic pressure of the molten core of the strand 2 is then enhanced.
Tin and zinc are partic~larly well-suited as the substance 5 for the casting of steel. Other materials which may be used as the substance 5 for 25 the casting of steel are the alloys of tin, e.g. 97 Sn-3 Cu and 67.8 Sn-33 Cd; ~he alloys of zinc, e.g.
95 Zn-5 Al; indium and its alloys, e.g. 97 In-3 Ag;
and lead-based alloys, e.g. 43 Pb-43 Sn-14 Bi.
The casting apparatus of FIG. 1 is assumed 3Q to be a single-strand machine. However~ the invention is equally applicable to multiple-strand machines. This is schematically illustratea in FIG.
2 where a pair of strands 2a,2b formed in a two-strand casting apparatus are adva~ced through a 35 common bath of the substance 5. Alternatively to the c ~ s~ ( _ - 23 -~_ ......

,, . . . ~ . . ~. .
- 1 showing of FIG. 2, a separate tank 4 and a separate ba~h of the substance 5 may be providea for each of the s~rands 2a,2b. If a casting apparatus has more than two strands, a single tank 4 or any suitable distribution of a plurality of tanks 4 may be used to cool the various strands.
The skids 8 of FIG. 1 may be replaced by rollers 7a. As illustrated in FIG. 3a, the guide rollers 7a,7b may be cantilevered. Each of the guide rollers 7a,7b of FIG. 3a is designed in such a manner as to only partially traverse the path A of the strand 2 so that the latter is supported at its marginal regions but not at its central region. On the other hand, FIG~ 3b shows that it is possible for ; 15 the guide rollers 7a,7b to be supported at both end~
and to traverse the path A completely thereby ; supporting the strand 2 across its width. A
combination of cantilevered and non-cantilevered guide rollers may also be used.
FIGS. 4a and 4b show that the strand 2 may be supp~rted on both sides by skids 8a,8b. In FIG.
4a, the skids 8a,8b are mounted in cantilever fashion and are designed so that they extend only partly across the path A of the strand 2. The strand 2 is thus supported at its marginal regions but is unsupported at its central region. In FIG. 4b, on the contrary, each skid 8a,8b is supported at either end and extends across the full width of the path A
so that the strand 2 is supported over its width.
3D FIG. 5 illustrates a continuous casting apparatus which generally resembles that of FIG. 1.
However, the heating and circulating units 12 of FIG.
1 are replaced by heating elements 18~ e.g.
resistance elements, and circulating pumps 19 which are separate from the heating elements 18.
I

~ZS~i7~6 Furthermore, the continuous casting apparatus of Fig. 5 has heat exchangers 13a which are designed to generate steam.
The steam produced in the heat exchangers 13a may, for example, be used in the operation of plant utilities. The continuous casting apparatus of Fig. S acLditionally differs from the apparatus of Fig. 1 in that the withdrawal unit 10 and straightening section 7c of ~ig. 1 are combined in a single withdrawal and straightening unit 20. The withdrawal and straightening unit 20 is located in the substance 5 entirely. A drive unit 21 for the withdrawal and straightening unit 20 is disposed above the tank 4, e.g. on the casting platform. The withdrawal and straightening unit 20 is made up of several pairs oP cooperating rollers, and the drive unit 21 includes a separate motor ;Eor each pair o;E
rollers. Each motor is connected to at leas~ one roller of the respective roller p~r by a coupling mecllanism 22.
Fig. 6 shows a continuous casting apparatus similar to those of Figs.l and S. In the apparatus of Fig. 6, however, the strand 2 is not straightened in the bath of the substance 5 and maintains a constant curvature until it leaves the bath. The radius of curvature of the strand 2 as it travels through the bath is the casting radius R which is the radius of curvature of the casting passage la. ~y main-taining the curvature of the strand 2 throughout the bath, it becomes possible for the withdrawal and straightening unit 20 to be only partially immersed in the bath or to be located outside of the bath entirely.
This facilitates access to the withdrawal and straightening unit 20.
In contrast to the continuous casting apparatus of Figs. 1 and 5 where the torch unit 11 is .~

\f ' . ! , . ~ :

~ ~Z~à67~ ~

1 located to the side of the tank 4, the torch unit 11 in the apparatus of FIG. 6 is mounted above the tank

4 on a non-illustrated support. The cut sections of the strand 2 issuing from the torch unit ll in the apparatus of FIG; 6 may, for example, be removed from the apparatus via a crane. During the cutting operation, the section being cut may be gripped by the crane or by a pair of rollers to prevent it from falling once the cut has been completed.
FIG. 7 illustrates a continuous casting apparatus in which the curvature o~ the strand 2 is maintained throughout the bath of the substance 5 but which is designed so as to permit placement o~ the torch unit 11 to the side of the tank 4 rather than above the latter. ~o this end, the apparatus of FIG.
7 is provided with a bending unit 23 which reverses the curvature of the strand 2 thereby causing the strand 2 to travel towards the side of the tank 4 after leaving the bath. The bending unit 23 may be 20 partially immersed in the bath as shown or may be disposed outside of the bath in its entirety. The bending unit 23 is made up of pairs of cooperating rollers, and these rollers may all be idler rollers or may include at least one driven roller. If the 25 bending unit 23 is provided with one or more driven rollers, it may also function as a withdrawal unit.
A straightening unit 24 is located downstream of the bending unit 23 and serves to straighten the strand 2. The straightening unit 24, 30 which is optional, is again made up of pairs of cooperating rollers. The rollers of the straightening unit 24 may all be idler rollers or may include at least one driven roller. In the latter case, the straightening unit 24 may perform a 35 withdrawal function.

. :

C ~2~75~ ( , . .
r~-- - 26 -~ .~.~c ~ _ 1 The torch unit 11, which is not illustrated -~ in F~G. 7, is arranged downstream of the straightening unit 24 and hence to the side of the tank 4.
The apparatus of FIG. 7 inclu~es a ho~d 25 for the evacuation of fumes which may be generated by the bath of the substance 5. The hood 25, which is located above the tank 4, is provided with a blower 26. The blower 26 draws the fumes generated by the : 10 -bath into a duct 27 which leads to a conventional air purification system.
FIG. 8 shows a con~inuous casting apparatus which is similar to those of FIGS. 6 and 7 in that the curva~ure o~ the strand 2 is maintained throu~hout the bath of the substance 5. }lowever, contrary to the apparatus of FIGS. 6 and 7, the strand 2 in the apparatus of FIG. 8 is permitted to retain its curvature after leaving the bath so that the strand 2 turns back towards the mold 1. The withdrawal and straightening unit 20 which may, for example, be mounted on a special platform above the casting platform, is arranged to straighten the strand 2 before the latter again begins to travel downwards. The torch unit 11, which is not shown in FIG~ 8, is located downstream of the wlthdrawal and straightening unit 20 and may likewise be mounted on a special platform disposed at a level above the casting platform.
The path A followed by the strand 2 in the apparatus of FIG. 8 passes directly over the mold 1.
Normally, the space directly above the mold 1 is o~cupiea by the ladle 16 during casting. In order to prevent obstruction of the strand 2 by the ladle 16, the latte~ may be shiftea to one side of the mold 1 35 as illustratea in FI~. 9. The tundish 15 i5 then C ~ 5G, (~

~ 27 , . _ . .. ,~ . . .
- -1 positioned in ~uch a manner tha~ one end thereof is situated above the mold 1 while the other end is located below the ladle 16. This enables the molten metal to be teemed from the ladle 16 into the mold 1

5 ~ia the tundish 15 even though the ladle 16 has been shifted to one side of the mold 1.
FIG. 10 shows a continuous casting apparatus in which heat is removed from the bath of the : substance 5 through the peripheral wal~s of the tank 10 4. The peripheral walls of the tank 4 in the apparatus of FIG. 10 are uninsulated. In order to accelerate the removal of heat ~rom the bath, the pecipheral walls of the tank 4 may be provided with cooling fins 28. Moreover, ventilators 29 fo~
15 foecing cool air over the ins 28 may be mountecl on or adjacent to the peripheral walls of the tank 4.
It is possible to omit heat exchangers from the tank 4 in the apparatus of FIG. 10. ~owever, if further acceleration in the removal of heat from the 20 bath of the substance 5 is desired, this may be ~accomplished by placing heat exchangers in the tank 4.
; . In the apparatus of FIG. 10, the outlet end lc of the mold 1 is located above the upper surface 6 of the substance 5. The outlet end lc may, of 25 course, be similarly positioned in the apparatus of FIGS. 1 and 5-9 while, conversely, the outlet end lc in the apparatus of FIG. 10 may be located at or below the upper surface 6 of the substance 5.
FIGS. 11 and 12 illustrate a continuous 30 casting apparatus in which the tank 4 is replaced by a pipe 30. The interior of the pipe 30 accommodates the substance 5 for cooling the strand ~ formed in the mold 1. The interior of the pipe 30 further accommodates guide means for the strand 2. The guide 35 means is here in the form of skids 8c arranged to :~6675G C

, r~ 28 -1 engage that surface of the strand 2 which forms adjacent to the inner radius of the casting passage la, and skids 8d arranqed to engage that surface of the strand 2 which forms adjacent to the outer radius S of the casting passage la. The skids 8c and 8d, which are shown as engaging only the marginal regions of the strand 2, are secured to the inner surface of the pipe 30, e.g. by welding.
The pipe 30 has an inlet end 30a through which the strand 2 enters the pipe 30, and an outlet end 30b via which the strand 2 exits from the pipe 30. the inlet end 30a i5 closed except for an opening dimensioned to snugl~ receive the outlet end lc of the mold 1. Similarl~, the outlet end 30b is closed except ~or an opening through which the strand 2 is withdrawn from the pipe 30. The pipe 30 has a curvature which corresponds to that of the casting passage la, and hence to the curvature of the strand 2.
Heating elements 18 are disposed internally of the pipe 30 in order to supply heat to the substance 5. Although not illustrated in FIGS~ 11 and 12, it is further possible to place circulating pumps inside the pipe 30 to effect circulation of the bath formed by the substance 5. Combined heating and circulating units such as shown at 12 in FIG. 1 may also be employed in the pipe 30.
The apparatus of FIGS. 11 and 12 is designed for the recovery of heat from the strand 2. To this end, a heat exchange system is located inside ~he pipe 30. ~he heat exchange system includes a series of conduits 13b which extend lengthwise of the pipe 30 and carry a cooling fluid, e.g. water. In order to ~educe heat losses through the walls of the pipe 30, the latter is surrounded by an insulating jacket :~2~75~ c ~ 29--~ ,_ .

1 31.
If ~eat recovery from the strand 2 is not desired, the insulating jacket 31 may be eliminated and the pipe 30 provided with cooling fins such as 5 shown at 28 in FIG. 10. Ventilators like those identified at 29 in FIG. 10 may then also be disposed adjacent to the pipe 30.
A pair of diametrically opposed flanges 34 is formed on the pipe 30. The flanges 34 rest on a 10 base 32 which serves to support the pipe 30. Added support for the pipe 30 may be provided by a series of columns 33 which are spaced along the base 32 and engage the pipe 30 from below.
The pipe 30 i5 illust~ted as havincJ a 15 circular cross section. However, this i8 b~ way of example only r and the pipe 30 may have any other type of cross section, e.g. polygonal.
The continuous casting apparatus of FIGS. 11 and 12 has the advantage that cooling of the strand 2 20 may be achieved using smaller amounts of the substance 5 than in the apparatus of FIGS. 1, 2 and 5-10. In addition to the savings in material which may be realized by using smaller amounts of the substance 5, energy costs may be reduced since less 25 energy is required to heat the substance 5 and maintain it at temperature prior to and between casts. Moreover, the time required to heat the substance 5 may be reduced. Another advantage of the apparatus of FIGS. 11 and 12 is that less surface 30 area of the substance 5 is exposed to the atmosphere.
The manner in which the heating and circulating units 12, the heating elements 18 and the pumps 19 are connected with external power sources via the walls of the tank 4 and the pipe 30 does not 35 form part of the invention per se, and conventional ~ ! ~L26~75~ C:
;,` -. .

. . .
.
tat~on~ry seals may be used for this purpose. The same applies to the manner in which the conduits of the heat exchan~ers 13,13a,13b are passed through the walls of the tank 4 and the pipe 30.
In continuous casting apparatus such as those illustrated in FIGS. 5 and 10 where driven rollers are located inside the tank 4, the rollers may be rotated by motors located either above or to the side of the ~ank 4. If the motors are situated -to the side of the tank 4, conventional dynamic seals may be employed to couple the motors with the driven rollers via a wall of the tank 4.
Situations may arise where it is desirable to use a substance 5 having a speci~ic gravity which is signi~icantly lower than that o~ the material being cast. Under such circumstances, a supply of the substance 5 may be confined in a vessel which is located at a level above and is in communication with the tank 4 or the pipe 30. The additional head of the substance 5 obtained in this manner may partially or entirely compensate for the difference in specific gravity depending upon the magnitude of the difference and the height differential of the vessel and the mold 1. This, in turn, enables better confinement of the molten core vf the strand 2 to be achieved. The tank 4 or pipe 30 must be appropriately sealed in order to prevent escape of the bath formed by the substance 5.
Although the invention has been described 30 with reference to vertical continuous casting apparatus, the invention is applicable to horizontal as well as other types of continuous casting apparatus.

.

~ .

~61~75~i . .

-- 1 Without further analysis, the foregoing will ~o fully reveal the gist of the present invention : that others can~ by applying current knowledge, readily aaapt it for various applications without 5 omittinq features that, from the standpoint of prior art, fairly constitute essential characteristics of the generic and specific aspects of our contribution to the art and, therefore, such ada]ptations should and are intended to be comprehended within the 10 meaning and range of equivalence of the appended claims~

Claims (32)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. A continuous casting apparatus comprising:
(a) a mold provided with a casting passage having an inlet end for molten material, and an outlet end for a continuously cast strand of the material, said mold being designed for the continuous casting of steel;
(b) withdrawal means for withdrawing the strand from said mold and conveying the strand along a predetermined path; and (c) cooling means for cooling the strand downstream of said mold, said cooling means including container means, and a non-gaseous cooling substance in said container means surrounding and contacting at least a portion of said path, said substance being capable of adhering to the strand so as to form a coating on the latter, and said substance having a boiling point lower than the melting point of the strand to thereby permit removal of the coating by heating, said substance comprising zinc.

2. The apparatus of claim 1, wherein the melting point of said substance is at most about 500°C.

3. The apparatus of claim 1, wherein said cooling means comprises heat exchanger means in contact with said substance.

4. The apparatus of claim 1, comprising heating means for melting said substance.

5. The apparatus of claim 9, wherein said heating means is disposed in said substance.

6. The apparatus of claim 1, comprising circulating means for circulating said substance when the latter is in liquid form.

7. The apparatus of claim 6, wherein said circulating means is disposed in said substance.

8. The apparatus of claim 1, comprising guide means for the strand, at least a portion of said guide means being disposed in said substance.

9. The apparatus of claim 8, wherein said guide means comprises skids.

10. The apparatus of claim 8, wherein said guide means comprises rollers.

11. The apparatus of claim 1, said mold being curved so that the strand has a curvature upon issuing from said mold; and further comprising straightening means for the strand, at least a portion of said straightening means being disposed in said substance.

12. The apparatus of claim 1, wherein at least a portion of said withdrawal means is disposed in said substance.

13. The apparatus of claim 12, said withdrawal means including at least one driven roller; and wherein said roller is disposed in said substance.

14. The apparatus of claim 1, wherein said container means comprises a tank.

15. The apparatus of claim 1, wherein said container means comprises a tube.

16. The apparatus of claim 1, comprising insulating means for said container means.

17. The apparatus of claim 1, said container means having a peripheral wall; and wherein said cooling means comprises removing means for removing heat from said peripheral wall.

18. The apparatus of claim 17, wherein said removing means comprises cooling fins on said peripheral wall.

19. The apparatus of claim 1, comprising exhaust means for exhausting fumes from said container means.

20. A continuous casting method comprising the steps of:
(a) continuously introducing molten material into one end of a casting passage having another end which is spaced from said one end;
(b) cooling said material in said passage to form a continuously cast strand;
(c) continuously withdrawing said strand from said passage via said other end;
(d) cooling said strand subsequent to withdrawal from said passage by immersing said strand in a bath, said bath including a substance capable of adhering to said strand; and (e) withdrawing said strand from said bath while said substance adheres thereto so that said substance forms a coating on said strand, said substance having a boiling point lower than the melting point of said strand to thereby permit removal of said coating by heating.

21. The method of claim 20, wherein said material comprises steel and said substance comprises zinc.

22. The method of claim 20, wherein said substance comprises a metal.

23. The method of claim 20, wherein said substance has a melting point of at most about 500°C.

24. The method of claim 20, wherein the strand cooling step comprises removing heat from said bath.

25. The method of claim 24, wherein the removing step comprises effecting indirect heat exchange between said bath and a cooling medium.

26. The method of claim 20, comprising the strand step of solidifying said bath subsequent to the cooling step.

27. The method of claim 20, comprising the step of circulating said bath.

28. The method of claim 20, comprising the step of guiding said strand in said bath.

29. The method of claim 20, said passage being curved so that said strand has a curvature upon issuing from said passage; and further comprising the step of at least partially straightening said strand in said bath.

30. The method of claim 20, wherein the second withdrawing conveying step comprises exerting a withdrawal force on said strand in said bath.

31. The method of claim 20, comprising the step of exhausting fumes from said bath.

32, The method of claim 20, comprising the step of supplying heat to said bath prior or subsequent to the strand cooling step to prevent solidification of said bath.