US2837790A - Process for degassing ferrous metals - Google Patents
Process for degassing ferrous metals Download PDFInfo
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- US2837790A US2837790A US400681A US40068153A US2837790A US 2837790 A US2837790 A US 2837790A US 400681 A US400681 A US 400681A US 40068153 A US40068153 A US 40068153A US 2837790 A US2837790 A US 2837790A
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- metal
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- barometric leg
- molten metal
- degassing
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- 229910052751 metal Inorganic materials 0.000 title claims description 70
- 239000002184 metal Substances 0.000 title claims description 70
- 238000000034 method Methods 0.000 title claims description 14
- 238000007872 degassing Methods 0.000 title claims description 13
- -1 ferrous metals Chemical class 0.000 title claims description 10
- 238000009749 continuous casting Methods 0.000 claims description 15
- 230000005484 gravity Effects 0.000 claims description 9
- 238000011109 contamination Methods 0.000 claims description 7
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 5
- 239000010959 steel Substances 0.000 description 5
- 238000009849 vacuum degassing Methods 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910001208 Crucible steel Inorganic materials 0.000 description 1
- 229910001141 Ductile iron Inorganic materials 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009851 ferrous metallurgy Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
- B22D11/11—Treating the molten metal
- B22D11/113—Treating the molten metal by vacuum treating
Definitions
- This invention deals with ferrous metallurgy and more particularly with an improvement upon the well known process of continuously casting ferrous metals.
- Figure 1 is a vertical section through one form of the apparatus of this invention
- FIG. 2 is a portion of another form of this invention.
- FIG. 3 is still another section of another phase of this invention.
- a stream of molten metal 10 is seen flowing from container 11 into the degassing apparatus which is generally indicated 12.
- This degassing apparatus is lined throughout with a refractory 13 and is heated as required by conductors 14 which heat the metal passing through the degassing apparatus either by an induction effect or by ordinary resistance heating, de-
- conductors 14 will take the form of tubing through which cooling water may be circulated as is conventional in high frequency induction heating.
- Metal 10 falling from container 11 is caught in tapered receptacle 15 which terminates at its lower end in nozzle 16 which is provided with a restricted throat 17.
- Throat 17 opens into vacuum degassing chamber 18 which, in common with the rest of the apparatus, is provided with a refractory lining 13.
- the vacuum de gassing chamber 18 is evacuated through conduit 19 connected to any vacuum producing apparatus, not shown.
- the lower portion of vacuum degassing chamber 18 connects with conduit 20, the purpose of which will be 'described.
- the metal 10 which falls from container 11 collects in tapered receptacle 15 and from there flows through nozzle 16 into vacuum degassing chamber 18.
- the metal passing through nozzle throat 17 is shattered and broken into a very large number of droplets which fall freely under the influence of gravity to the bottom of vacuum degassing chamber 18.
- vacuum chamber 18 which is maintained under a pressure from a few microns up to twenty millimeters of mercury, the metal is practically free of pressure except that exerted by surface tension.
- the metal is effectively degassed of such materials as nitrogen and hydrogen and the reaction between the iron oxide and carbon to produce carbon monoxide and iron is caused to occur with the simultaneous elimination of carbon and oxygen.
- the chemical analysis of the final product may advantageously be altered by the addition to the metal prior to its entrance into degassing chamber 18 of material which is capable of reacting with the charge to produce volatile reaction products, or reaction products which can be tolerated in the final product or reaction products capable of gravity separation in chamber 18.
- material which is capable of reacting with the charge to produce volatile reaction products, or reaction products which can be tolerated in the final product or reaction products capable of gravity separation in chamber 18.
- carbon may be added to the metal in tapered receptacle 15 so that the elimination of carbon by reaction with the iron oxide content of the melt in chamber 18 will leave the desired carbon residue.
- metallic compounds such as oxides may be added to alloy the product or add to the yield. Typical oxides are iron oxide and nickel oxide.
- gaseous purifying substances may be introduced through conduit 20 and exhausted through conduit 19 with the products of reaction.
- These rectifying metals may well be any of the volatile highly reactive metals such as magnesium, barium, strontium, calcium, lithium, sodium or potassium. These metals, due to the high heat of formation of their sulfides and oxides even at steel pouring temperatures, result in a product extremely low in sulphur and oxygen. By virtue of their low specific gravity, the reaction products produced within chamber 18 will float on the ceremoniesne metal and a separation thereby effected.
- barometric leg 21 The droplets of molten metal falling freely through vacuum degassing chamber 18 are again collected as a mass of ceremoniesne metal in the tapered bottom portion of this chamber which terminates in barometric leg 21.
- This barometric leg must, of course, be lined with refractory and in most instances must be provided with heating means to compensate for loss of temperature of the metal, at least upon starting.
- Barometric leg 21 must be sufficiently long to enable the ferrostatic head developed therein to equal the existing barometric pressure plus the frictional loss through the system.
- the apparatus is provided with a bott 22 arranged to close off the bottom of barometric leg 21 and to be moved into position by lever system 23. From the bottom of barometric leg 21 the metal enters the top of continuous casting apparatus generally indicated by 24.
- This continuous casting apparatus 24 comprises a mold 25 connected to barometric leg 21 by bellows 26. Bellows 26 are protected from the thermal action of the molten metal by telescoping radiation shields 27. Pipes.
- Mold may be any. of the molds described in the patent literature as suitable for continuously forming molten iron or steel into a bar. It is not considered necessary to detail mold 25 since the patent and current literature are very rich in such descriptions.
- Figure 2 represents a variation of Figure 1 in which the starting bott 22 and the argon purge apparatus is deleted and the metal passes directly from bell mouthed end of barometric leg 21 into continuous casting mold 25. This results in a decided simplification of the apparatus described in Figure 1 and in some cases may result in economies.
- Figure 3 presents a variation of Figures l and 2.
- the bell mouthed portion 38 of barometric leg 21 which is similar to that shown in Figure 2 except it is turned through a 90 degree angle. This turn eliminates the necessity for the excessively high structures usually associated with continuous casting apparatus and permits the solidifying metal to be fed directly into the rolling machinery.
- the solidifying metal within continuous casting apparatus 25 has been depicted in the conical shape usually assumed.
- This method and apparatus has been described as primarily intended for use with ordinary carbon steel; however, it is by no means so limited and may be applied to any material which it is desired to degas and purify. Such materials may well be cast iron or alloy steels. In the case of cast -iron, the purifying material may also serve as a nodularizing agent and enable the direct production of nodular iron without further addition agents.
- a process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into ceremoniesne metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
- a process for degassing ferrous metals comprising establishing a body of molten ferrous metal, adding a carbonaceous material to the molten body, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into ceremoniesne metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
- a process for degassing ferrous metals comprising establishing a body of molten ferrous metal, adding a material to the molten body capable of reacting therewith to produce a volatile product, flowing the molten 4 metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these'discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into ceremoniesne metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being prot d from gaseous contamination after it leaves the barometric leg.
- a process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete drop lets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, flowing vapors of a volatile reactive metal past said droplets, coalescing the discrete droplets into ceremoniesne metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
- a continuous casting machine comprising a receptacle for molten metal, an enlarged chamber connected to said receptacle via a restricted nozzle, a barometric leg communicating with the enlarged chamber and a continuous casting mold below and communicating with the end of the barometric leg remote from the enlarged chamber.
- a process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a'restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated cham ber, flowing a gaseous purifying substance past said droplets, coalescing the discrete droplets into ceremoniesne metal 'in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
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- Mechanical Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
June 10, 1958 w. ROZIAN 2,337,790 PROCESS FOR DEGASSING FERROUS METALS 7 Filed Dec. 28, less :wyawmw III A TTORNEYS United States Patent 2,837,790 PROCESS FOR DEGASSING FERROUS METALS Irving W. Rozian, Detroit, Mich., assignor to Ford Motor Company, Dearborn, Mich, a corporation of Delaware Application December 28, 1953, Serial No. 460,681
6 Claims. (Cl. 22--57.2)
This invention deals with ferrous metallurgy and more particularly with an improvement upon the well known process of continuously casting ferrous metals. There has been much work done in the-past decade upon processes for continuously casting molten steel into bar form which may be rolled directly into finished shapes without the necessity of going through the usual procedure of casting an ingot, reheating the ingot and rolling the heated ingot into bars.
Steel produced by this process has shown excellent physical properties and is adaptable for most uses. How ever, continuously cast steel bars cannot be used for'purposes requiring a fine surface finish due to the presence of seed shaped cavities just under the cast surface. The origin of these cavities is obscure but it is believed that they are caused by the release of gas from the metal during solidification. The instant invention has been evolved to avoid this difliculty and also to produce a thoroughly deoxidized and desulphurized product having superior properties due to the almost quantitative absence of oxygen and sulphur as well as the more inert constituents such as nitrogen and hydrogen in the finished,
product.
This invention is probably understood best by reference to the drawings in which:
Figure 1 is a vertical section through one form of the apparatus of this invention,
Figure 2 is a portion of another form of this invention, and
Figure 3 is still another section of another phase of this invention.
Turning to Figure 1, a stream of molten metal 10 is seen flowing from container 11 into the degassing apparatus which is generally indicated 12. This degassing apparatus is lined throughout with a refractory 13 and is heated as required by conductors 14 which heat the metal passing through the degassing apparatus either by an induction effect or by ordinary resistance heating, de-
pending upon the requirements of the specific instance. It is, of course, to be understood that if the metal is to be heated inductively, conductors 14 will take the form of tubing through which cooling water may be circulated as is conventional in high frequency induction heating. Metal 10 falling from container 11 is caught in tapered receptacle 15 which terminates at its lower end in nozzle 16 which is provided with a restricted throat 17. Throat 17, opens into vacuum degassing chamber 18 which, in common with the rest of the apparatus, is provided with a refractory lining 13. The vacuum de gassing chamber 18 is evacuated through conduit 19 connected to any vacuum producing apparatus, not shown. The lower portion of vacuum degassing chamber 18 connects with conduit 20, the purpose of which will be 'described.
The metal 10 which falls from container 11 collects in tapered receptacle 15 and from there flows through nozzle 16 into vacuum degassing chamber 18. The metal passing through nozzle throat 17 is shattered and broken into a very large number of droplets which fall freely under the influence of gravity to the bottom of vacuum degassing chamber 18. During their free fall through vacuum chamber 18, which is maintained under a pressure from a few microns up to twenty millimeters of mercury, the metal is practically free of pressure except that exerted by surface tension. During this period the metal is effectively degassed of such materials as nitrogen and hydrogen and the reaction between the iron oxide and carbon to produce carbon monoxide and iron is caused to occur with the simultaneous elimination of carbon and oxygen. The chemical analysis of the final product may advantageously be altered by the addition to the metal prior to its entrance into degassing chamber 18 of material which is capable of reacting with the charge to produce volatile reaction products, or reaction products which can be tolerated in the final product or reaction products capable of gravity separation in chamber 18. For example carbon may be added to the metal in tapered receptacle 15 so that the elimination of carbon by reaction with the iron oxide content of the melt in chamber 18 will leave the desired carbon residue. Conversely metallic compounds such as oxides may be added to alloy the product or add to the yield. Typical oxides are iron oxide and nickel oxide.
For further rectification of the metal, gaseous purifying substances may be introduced through conduit 20 and exhausted through conduit 19 with the products of reaction. These rectifying metals may well be any of the volatile highly reactive metals such as magnesium, barium, strontium, calcium, lithium, sodium or potassium. These metals, due to the high heat of formation of their sulfides and oxides even at steel pouring temperatures, result in a product extremely low in sulphur and oxygen. By virtue of their low specific gravity, the reaction products produced within chamber 18 will float on the reguline metal and a separation thereby effected.
The droplets of molten metal falling freely through vacuum degassing chamber 18 are again collected as a mass of reguline metal in the tapered bottom portion of this chamber which terminates in barometric leg 21. This barometric leg must, of course, be lined with refractory and in most instances must be provided with heating means to compensate for loss of temperature of the metal, at least upon starting. Barometric leg 21 must be sufficiently long to enable the ferrostatic head developed therein to equal the existing barometric pressure plus the frictional loss through the system. For starting purposes, the apparatus is provided with a bott 22 arranged to close off the bottom of barometric leg 21 and to be moved into position by lever system 23. From the bottom of barometric leg 21 the metal enters the top of continuous casting apparatus generally indicated by 24.
This continuous casting apparatus 24 comprises a mold 25 connected to barometric leg 21 by bellows 26. Bellows 26 are protected from the thermal action of the molten metal by telescoping radiation shields 27. Pipes.
28 and 29 are provided for the entry and exit of a purging gas such as argon or helium which serve to protect the degasified metal from contamination prior to solidification in mold 25. The pressure within bellows 26 will probably be substantially atmospheric although this is not necessary and it may be varied either above or below atmospheric as required. In any event, the length of barometric leg 21 must be adjusted with the pressure in bellows 26 in mind. The diameter of the conduit provided for the flow of metal through barometric leg 21 must be chosen in relationship to the amount of metal per unit time to pass through so that the downward velocity of the metal exceeds the velocity at which a bubble of the gas within bellows 26 could rise through the metal being handled.
Mold may be any. of the molds described in the patent literature as suitable for continuously forming molten iron or steel into a bar. It is not considered necessary to detail mold 25 since the patent and current literature are very rich in such descriptions.
Figure 2 represents a variation of Figure 1 in which the starting bott 22 and the argon purge apparatus is deleted and the metal passes directly from bell mouthed end of barometric leg 21 into continuous casting mold 25. This results in a decided simplification of the apparatus described in Figure 1 and in some cases may result in economies.
Similarly, Figure 3 presents a variation of Figures l and 2. Here again occurs the bell mouthed portion 38 of barometric leg 21 which is similar to that shown in Figure 2 except it is turned through a 90 degree angle. This turn eliminates the necessity for the excessively high structures usually associated with continuous casting apparatus and permits the solidifying metal to be fed directly into the rolling machinery. In each case the solidifying metal within continuous casting apparatus 25 has been depicted in the conical shape usually assumed.
This method and apparatus has been described as primarily intended for use with ordinary carbon steel; however, it is by no means so limited and may be applied to any material which it is desired to degas and purify. Such materials may well be cast iron or alloy steels. In the case of cast -iron, the purifying material may also serve as a nodularizing agent and enable the direct production of nodular iron without further addition agents.
I claim as my invention:
1. A process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into reguline metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
2. A process for degassing ferrous metals comprising establishing a body of molten ferrous metal, adding a carbonaceous material to the molten body, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into reguline metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
3. A process for degassing ferrous metals comprising establishing a body of molten ferrous metal, adding a material to the molten body capable of reacting therewith to produce a volatile product, flowing the molten 4 metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these'discrete droplets to descend under the influence of gravity through the evacuated chamber, coalescing the discrete droplets into reguline metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being prot d from gaseous contamination after it leaves the barometric leg.
4. A process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a restricted nozzle into an evacuated chamber whereby it is shattered into discrete drop lets, permitting these discrete droplets to descend under the influence of gravity through the evacuated chamber, flowing vapors of a volatile reactive metal past said droplets, coalescing the discrete droplets into reguline metal in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
5. A continuous casting machine comprising a receptacle for molten metal, an enlarged chamber connected to said receptacle via a restricted nozzle, a barometric leg communicating with the enlarged chamber and a continuous casting mold below and communicating with the end of the barometric leg remote from the enlarged chamber.
6. A process for degassing ferrous metals comprising establishing a body of molten ferrous metal, flowing the molten metal through a'restricted nozzle into an evacuated chamber whereby it is shattered into discrete droplets, permitting these discrete droplets to descend under the influence of gravity through the evacuated cham ber, flowing a gaseous purifying substance past said droplets, coalescing the discrete droplets into reguline metal 'in the lower portion of the evacuated chamber, withdrawing molten metal from the evacuated chamber through a barometric leg and discharging the barometric leg into a continuous casting mold, said molten metal being protected from gaseous contamination after it leaves the barometric leg.
References Cited in the file of this patent UNITED STATES PATENTS 211,953 Barnum Feb. 4, 1879 448,945 Durfee et a1 Mar. 24, 1891 1,568,854 Larner Jan. 5, 1926 1,590,730 Evans June 29, 1926 1,633,992 Madden June 28, 1927 2,253,421 De Mare Aug. 19, 1941 2,303,139 Roemer Nov. 24, 1942 2,587,793 Waldron Mar. 4, 1952 2,590,311 Hatter et al. Mar. 25, 1952 2,625,472 Scheuer Jan. 13, 1953 2,709,842 Findley June 7, 1955 2,734,240 0 Southern Feb. 14, 1956 FOREIGN PATENTS 891,444 Germany Sept. 28, 1953
Claims (2)
1. A PROCESS FOR DEGASSING FERROUS METALS COMPRISING ESTABLISHING A BODY OF MOLTEN FERROUS METAL, FLOWING MOLTEN METAL THROUGH A RESTRICTED NOZZLE INTO AN EVACUATED CHAMBER WHEREBY IT IS SHATTERED INTO DISCRETE DROPLETS, PERMITTING THESE DISCRETE DROPLETS TO DESCEND UNDER THE INFLUENCE OF GRAVITY THROUGH THE EVACUTTED CHAMBER, COALESCING THE DISCRETE DROPLETS INTO REGULINE METAL IN THE LOWER PORTION OF THE EVACUTATED CHAMBER, WITHDRAWING MOLTEN METAL FROM THE EVACUATED CHAMBER THROUGH A BAROMETRIC LEG AND DISCHARGING THE BAROMETRIC LEG INTO A CONTINUOUS CASTING MOLD, SAID MOLTEN METAL BEING PROTECTED FROM GASEOUS CONTAMINATION AFTER IT LEAVES THE BAROMETRIC LEG.
5. A CONTINUOUS CASTING MACHINE COMPRISING A RECEPTACLE FOR MOLTEN METAL, AN ENLARGED CHAMBER CONNECTED TO SAID RECEPTACLE VIA A RESTRICTED NOZZLE, A BAROMETRIC LEG COMMUNICATING WITH THE ENLARGED CHAMBER AND A CONTINUOUS CASTING MOLD BELOW AND COMMUNICATING WITH THE END OF THE BAROMETRIC LEG REMOTE FROM THE ENLARGED CHAMBER.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US400681A US2837790A (en) | 1953-12-28 | 1953-12-28 | Process for degassing ferrous metals |
| FR1115577D FR1115577A (en) | 1953-12-28 | 1954-10-07 | Process for degassing metals in a vacuum, and apparatus for carrying out said process |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US1115577XA | 1953-12-28 | 1953-12-28 | |
| US763872XA | 1953-12-28 | 1953-12-28 | |
| US400681A US2837790A (en) | 1953-12-28 | 1953-12-28 | Process for degassing ferrous metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2837790A true US2837790A (en) | 1958-06-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US400681A Expired - Lifetime US2837790A (en) | 1953-12-28 | 1953-12-28 | Process for degassing ferrous metals |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US2837790A (en) |
| FR (1) | FR1115577A (en) |
Cited By (41)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2906521A (en) * | 1956-03-16 | 1959-09-29 | Hoerder Huettenunion Ag | Sealing means for vacuum vessels |
| US2993780A (en) * | 1957-11-16 | 1961-07-25 | Siderurgie Fse Inst Rech | Method for treating steel in vacuo |
| US2997386A (en) * | 1958-06-27 | 1961-08-22 | Feichtinger Heinrich | Process and apparatus for treating metal melts |
| US3013316A (en) * | 1958-12-31 | 1961-12-19 | United States Steel Corp | Method and apparatus for vacuum casting |
| US3014255A (en) * | 1957-11-15 | 1961-12-26 | Heraeus Gmbh W C | Method of operating vacuum induction furnace |
| US3026195A (en) * | 1957-03-26 | 1962-03-20 | Edstrom John Olof | Method of degasifying steel and other metals |
| US3050798A (en) * | 1960-06-13 | 1962-08-28 | Strategic Materials Corp | Process for continuous casting and vacuum degasification |
| US3071362A (en) * | 1958-05-30 | 1963-01-01 | Heraeus Gmbh W C | Immersion pipe for degassing metals by a vacuum |
| US3078695A (en) * | 1958-04-23 | 1963-02-26 | Kimble Glass Co | Apparatus for extruding glass |
| US3084038A (en) * | 1959-11-25 | 1963-04-02 | Finkl & Sons Co | Method and apparatus for combined stream and ladle degassing |
| US3099053A (en) * | 1959-03-25 | 1963-07-30 | Olin Mathieson | Apparatus and process for continuous casting |
| US3125440A (en) * | 1960-12-27 | 1964-03-17 | Tlbr b | |
| US3146503A (en) * | 1961-01-24 | 1964-09-01 | Bochumer Ver Fuer Gusstahlfabr | Degasification of metal |
| DE1188105B (en) * | 1960-10-07 | 1965-03-04 | Bochumer Ver Fuer Gusstahlfabr | Process for casting jet degassing of steel melts intended for the production of continuous castings |
| US3179512A (en) * | 1961-08-09 | 1965-04-20 | Olsson Erik Allan | Method for transporting and degasifying a melt |
| US3180633A (en) * | 1962-07-18 | 1965-04-27 | Pennsalt Chemicals Corp | Apparatus for producing ultraclean alloy steels |
| US3206301A (en) * | 1959-11-23 | 1965-09-14 | Metallurg D Esperance Longdoz | Process for the continuous treatment of steel |
| US3212881A (en) * | 1962-12-04 | 1965-10-19 | Westinghouse Electric Corp | Purification of alloys |
| DE1213963B (en) * | 1962-07-11 | 1966-04-07 | Demag Ag | Device for evacuating the casting and distribution system during the continuous casting of steel or metal melts |
| US3281903A (en) * | 1964-02-03 | 1966-11-01 | Walter C Ross | Method and apparatus for continuous horizontal casting |
| US3309194A (en) * | 1964-12-24 | 1967-03-14 | Westinghouse Electric Corp | Purification of alloys |
| US3321008A (en) * | 1963-10-18 | 1967-05-23 | M E A Inc | Apparatus for the continuous casting of metal |
| US3332474A (en) * | 1963-03-02 | 1967-07-25 | Midvale Heppenstall Company | Apparatus and method for continuous vacuum degassing and casting of steel and other metals |
| US3333839A (en) * | 1963-10-02 | 1967-08-01 | Yawata Iron & Steel Co | Apparatus for recovering unburned gases issued from metal refining furnaces |
| DE1246001B (en) * | 1962-07-03 | 1967-08-03 | Hoerder Huettenunion Ag | Vacuum container for degassing metal, especially iron and steel melts |
| US3347538A (en) * | 1965-04-28 | 1967-10-17 | Mc Graw Edison Co | Apparatus for the vacuum degassing of molten metal |
| DE1271139B (en) * | 1961-01-24 | 1968-06-27 | Krupp Ag Huettenwerke | Method and device for degassing metal melts, in particular steel and cast iron melts |
| US3392009A (en) * | 1965-10-23 | 1968-07-09 | Union Carbide Corp | Method of producing low carbon, non-aging, deep drawing steel |
| US3399715A (en) * | 1964-09-22 | 1968-09-03 | Hoerder Huettenunion Ag | Method for the continuous casting of metal |
| US3402921A (en) * | 1965-08-30 | 1968-09-24 | Phelps Dodge Corp | Apparatus and method of making apparatus for vacuum purification of metals |
| DE1533949B1 (en) * | 1967-06-19 | 1971-01-28 | Standard Messo Duisburg | Device for the continuous production of vacuum steel from pig iron |
| US3581803A (en) * | 1968-05-24 | 1971-06-01 | Charles W Finkl | Method of reducing center porosity in ingot casting |
| US3779743A (en) * | 1972-04-24 | 1973-12-18 | United States Steel Corp | Continuous casting with in-line stream degassing |
| US3790369A (en) * | 1971-06-01 | 1974-02-05 | United States Steel Corp | Method for enhancing the reaction of a species of a liquid with a fluid substance |
| DE2929500A1 (en) * | 1979-07-20 | 1981-01-29 | Hamburger Stahlwerke Gmbh | Telescopic shroud for molten metal stream - esp. for providing gas curtain round stream of metal flowing into mould in continuous casting plant |
| US5366206A (en) * | 1993-12-17 | 1994-11-22 | General Electric Company | Molten metal spray forming atomizer |
| US5649993A (en) * | 1995-10-02 | 1997-07-22 | General Electric Company | Methods of recycling oversray powder during spray forming |
| US5649992A (en) * | 1995-10-02 | 1997-07-22 | General Electric Company | Methods for flow control in electroslag refining process |
| US5683653A (en) * | 1995-10-02 | 1997-11-04 | General Electric Company | Systems for recycling overspray powder during spray forming |
| US6250522B1 (en) | 1995-10-02 | 2001-06-26 | General Electric Company | Systems for flow control in electroslag refining process |
| US6425504B1 (en) * | 1999-06-29 | 2002-07-30 | Iowa State University Research Foundation, Inc. | One-piece, composite crucible with integral withdrawal/discharge section |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1212122B (en) * | 1960-08-08 | 1966-03-10 | Bochumer Ver Fuer Gussstahlfab | Process for the production of heat-treatable ferritic-pearlitic steels, primarily for heavy forgings |
| DE1262521B (en) * | 1960-09-19 | 1968-03-07 | Kind & Co Fa | Device for melting and casting metals under vacuum or low protective gas pressure |
| DE1233110B (en) * | 1961-12-23 | 1967-01-26 | Demag Ag | Method and device for the negative pressure treatment of metal or steel alloys |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US211953A (en) * | 1879-02-04 | Improvement in apparatus for casting metals | ||
| US448945A (en) * | 1891-03-24 | Sylvania | ||
| US1568854A (en) * | 1924-08-05 | 1926-01-05 | George E Fulton | Steel-casting apparatus |
| US1590730A (en) * | 1924-04-23 | 1926-06-29 | Mathieson Alkali Works | Method of desulphurizing iron |
| US1633992A (en) * | 1927-01-14 | 1927-06-28 | Bernard J Madden | Box for pouring steel ingots |
| US2253421A (en) * | 1938-09-20 | 1941-08-19 | Mare Baltzar E L De | Method and apparatus for deoxidizing and degasifying liquid steel |
| US2303139A (en) * | 1941-10-23 | 1942-11-24 | George R Roemer | Method of and apparatus for centrifugally degasifying molten metal |
| US2587793A (en) * | 1949-04-05 | 1952-03-04 | Waldron Frederic Barnes | Manufacture of steel |
| US2590311A (en) * | 1948-02-26 | 1952-03-25 | Babcock & Wilcox Co | Process of and apparatus for continuously casting metals |
| US2625472A (en) * | 1948-08-18 | 1953-01-13 | Aluminium Lab Ltd | Distillation of aluminum from aluminum alloys |
| DE891444C (en) * | 1942-09-02 | 1953-09-28 | Ver Leichtmetallwerke Gmbh | Device for simultaneous casting of several metal bars |
| US2709842A (en) * | 1951-07-06 | 1955-06-07 | Gordon R Findlay | Apparatus for continuous casting of high-melting-point metals |
| US2734240A (en) * | 1956-02-14 | Vacuum pouring apparatus |
-
1953
- 1953-12-28 US US400681A patent/US2837790A/en not_active Expired - Lifetime
-
1954
- 1954-10-07 FR FR1115577D patent/FR1115577A/en not_active Expired
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2734240A (en) * | 1956-02-14 | Vacuum pouring apparatus | ||
| US448945A (en) * | 1891-03-24 | Sylvania | ||
| US211953A (en) * | 1879-02-04 | Improvement in apparatus for casting metals | ||
| US1590730A (en) * | 1924-04-23 | 1926-06-29 | Mathieson Alkali Works | Method of desulphurizing iron |
| US1568854A (en) * | 1924-08-05 | 1926-01-05 | George E Fulton | Steel-casting apparatus |
| US1633992A (en) * | 1927-01-14 | 1927-06-28 | Bernard J Madden | Box for pouring steel ingots |
| US2253421A (en) * | 1938-09-20 | 1941-08-19 | Mare Baltzar E L De | Method and apparatus for deoxidizing and degasifying liquid steel |
| US2303139A (en) * | 1941-10-23 | 1942-11-24 | George R Roemer | Method of and apparatus for centrifugally degasifying molten metal |
| DE891444C (en) * | 1942-09-02 | 1953-09-28 | Ver Leichtmetallwerke Gmbh | Device for simultaneous casting of several metal bars |
| US2590311A (en) * | 1948-02-26 | 1952-03-25 | Babcock & Wilcox Co | Process of and apparatus for continuously casting metals |
| US2625472A (en) * | 1948-08-18 | 1953-01-13 | Aluminium Lab Ltd | Distillation of aluminum from aluminum alloys |
| US2587793A (en) * | 1949-04-05 | 1952-03-04 | Waldron Frederic Barnes | Manufacture of steel |
| US2709842A (en) * | 1951-07-06 | 1955-06-07 | Gordon R Findlay | Apparatus for continuous casting of high-melting-point metals |
Cited By (42)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2906521A (en) * | 1956-03-16 | 1959-09-29 | Hoerder Huettenunion Ag | Sealing means for vacuum vessels |
| US3026195A (en) * | 1957-03-26 | 1962-03-20 | Edstrom John Olof | Method of degasifying steel and other metals |
| US3014255A (en) * | 1957-11-15 | 1961-12-26 | Heraeus Gmbh W C | Method of operating vacuum induction furnace |
| US2993780A (en) * | 1957-11-16 | 1961-07-25 | Siderurgie Fse Inst Rech | Method for treating steel in vacuo |
| US3078695A (en) * | 1958-04-23 | 1963-02-26 | Kimble Glass Co | Apparatus for extruding glass |
| US3071362A (en) * | 1958-05-30 | 1963-01-01 | Heraeus Gmbh W C | Immersion pipe for degassing metals by a vacuum |
| US2997386A (en) * | 1958-06-27 | 1961-08-22 | Feichtinger Heinrich | Process and apparatus for treating metal melts |
| US3013316A (en) * | 1958-12-31 | 1961-12-19 | United States Steel Corp | Method and apparatus for vacuum casting |
| US3099053A (en) * | 1959-03-25 | 1963-07-30 | Olin Mathieson | Apparatus and process for continuous casting |
| US3206301A (en) * | 1959-11-23 | 1965-09-14 | Metallurg D Esperance Longdoz | Process for the continuous treatment of steel |
| US3084038A (en) * | 1959-11-25 | 1963-04-02 | Finkl & Sons Co | Method and apparatus for combined stream and ladle degassing |
| US3050798A (en) * | 1960-06-13 | 1962-08-28 | Strategic Materials Corp | Process for continuous casting and vacuum degasification |
| DE1188105B (en) * | 1960-10-07 | 1965-03-04 | Bochumer Ver Fuer Gusstahlfabr | Process for casting jet degassing of steel melts intended for the production of continuous castings |
| US3125440A (en) * | 1960-12-27 | 1964-03-17 | Tlbr b | |
| US3146503A (en) * | 1961-01-24 | 1964-09-01 | Bochumer Ver Fuer Gusstahlfabr | Degasification of metal |
| DE1271139B (en) * | 1961-01-24 | 1968-06-27 | Krupp Ag Huettenwerke | Method and device for degassing metal melts, in particular steel and cast iron melts |
| US3179512A (en) * | 1961-08-09 | 1965-04-20 | Olsson Erik Allan | Method for transporting and degasifying a melt |
| DE1246001B (en) * | 1962-07-03 | 1967-08-03 | Hoerder Huettenunion Ag | Vacuum container for degassing metal, especially iron and steel melts |
| DE1213963B (en) * | 1962-07-11 | 1966-04-07 | Demag Ag | Device for evacuating the casting and distribution system during the continuous casting of steel or metal melts |
| US3180633A (en) * | 1962-07-18 | 1965-04-27 | Pennsalt Chemicals Corp | Apparatus for producing ultraclean alloy steels |
| US3212881A (en) * | 1962-12-04 | 1965-10-19 | Westinghouse Electric Corp | Purification of alloys |
| US3332474A (en) * | 1963-03-02 | 1967-07-25 | Midvale Heppenstall Company | Apparatus and method for continuous vacuum degassing and casting of steel and other metals |
| US3333839A (en) * | 1963-10-02 | 1967-08-01 | Yawata Iron & Steel Co | Apparatus for recovering unburned gases issued from metal refining furnaces |
| US3321008A (en) * | 1963-10-18 | 1967-05-23 | M E A Inc | Apparatus for the continuous casting of metal |
| US3281903A (en) * | 1964-02-03 | 1966-11-01 | Walter C Ross | Method and apparatus for continuous horizontal casting |
| US3399715A (en) * | 1964-09-22 | 1968-09-03 | Hoerder Huettenunion Ag | Method for the continuous casting of metal |
| DE1458031B1 (en) * | 1964-09-22 | 1971-10-14 | Hoesch Ag | Method and device for continuous casting of metal |
| US3309194A (en) * | 1964-12-24 | 1967-03-14 | Westinghouse Electric Corp | Purification of alloys |
| US3347538A (en) * | 1965-04-28 | 1967-10-17 | Mc Graw Edison Co | Apparatus for the vacuum degassing of molten metal |
| US3402921A (en) * | 1965-08-30 | 1968-09-24 | Phelps Dodge Corp | Apparatus and method of making apparatus for vacuum purification of metals |
| US3392009A (en) * | 1965-10-23 | 1968-07-09 | Union Carbide Corp | Method of producing low carbon, non-aging, deep drawing steel |
| DE1533949B1 (en) * | 1967-06-19 | 1971-01-28 | Standard Messo Duisburg | Device for the continuous production of vacuum steel from pig iron |
| US3581803A (en) * | 1968-05-24 | 1971-06-01 | Charles W Finkl | Method of reducing center porosity in ingot casting |
| US3790369A (en) * | 1971-06-01 | 1974-02-05 | United States Steel Corp | Method for enhancing the reaction of a species of a liquid with a fluid substance |
| US3779743A (en) * | 1972-04-24 | 1973-12-18 | United States Steel Corp | Continuous casting with in-line stream degassing |
| DE2929500A1 (en) * | 1979-07-20 | 1981-01-29 | Hamburger Stahlwerke Gmbh | Telescopic shroud for molten metal stream - esp. for providing gas curtain round stream of metal flowing into mould in continuous casting plant |
| US5366206A (en) * | 1993-12-17 | 1994-11-22 | General Electric Company | Molten metal spray forming atomizer |
| US5649993A (en) * | 1995-10-02 | 1997-07-22 | General Electric Company | Methods of recycling oversray powder during spray forming |
| US5649992A (en) * | 1995-10-02 | 1997-07-22 | General Electric Company | Methods for flow control in electroslag refining process |
| US5683653A (en) * | 1995-10-02 | 1997-11-04 | General Electric Company | Systems for recycling overspray powder during spray forming |
| US6250522B1 (en) | 1995-10-02 | 2001-06-26 | General Electric Company | Systems for flow control in electroslag refining process |
| US6425504B1 (en) * | 1999-06-29 | 2002-07-30 | Iowa State University Research Foundation, Inc. | One-piece, composite crucible with integral withdrawal/discharge section |
Also Published As
| Publication number | Publication date |
|---|---|
| FR1115577A (en) | 1956-04-26 |
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