US1733522A - Apparatus for refining metals - Google Patents
Apparatus for refining metals Download PDFInfo
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- US1733522A US1733522A US166892A US16689227A US1733522A US 1733522 A US1733522 A US 1733522A US 166892 A US166892 A US 166892A US 16689227 A US16689227 A US 16689227A US 1733522 A US1733522 A US 1733522A
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- metal
- reagent
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- molten
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
Definitions
- This invention relates to metal refining, and, more particularly, to a method and apparatus for removing impurities from molten metals by the addition of a suitable reagent 5 thereto.
- the invention relates more specifically to the refining of'metals by passing them, in a molten condition, over a suitable surface to form a thin film, and adding the reagent to said film.
- the invention further consists in the new and novel features of operation and the new and original arrangementsand combinations of steps in the process hereinafter described and more particularly set forth in the claims.
- impurities b In certain types of metallurgical processes, for examplein the refining of lead, it is desirable to remove impurities b the addition of a suitable reagent for uniting with the impurities to produce a compound which floats upon the surface of the molten metal as a dross.
- impurities such as copper may be remove as a dross by reacting the molten metal with sulphur under suitable conditions for causing the sulphur to readily unite with the copper content of the metal.
- the molten metal is caused to pass, in a com aratively thin film, over a suitable surface.
- he reagent may be added to the flowing film, which presents a large surface area per unit of mass, and, by reason of the thin film. may be brought into intimate contact with the various portions of the metal. It may be further mixed with the metal by causing agitation of the film before returning the same to the bath.
- Fig. 1 is a diagrammatic representation of one orm of apparatus which may be employed in carrying out this process.
- Fig. 2 represents a modified form of mixing-chamber which may be employed therein.
- the material to be treated such as molten lead
- a suitable kettle 10 which is adapted to be heated by a furnace or other means (not shown).
- Molten metal may be removed from kettle 10 by means of centrifugal pump 11, which is supported in the lower portion of said kettle from beam 11', extendmg across and resting upon the rim of said kettle.
- Pump 11 may be driven by motor 12, which is supported by and carried upon said beam, and is driven by means of rod 13 connecting said motor and said pump.
- Suitable bracin means 14 may be employed, if desired, For maintaining pump 11 in the desired position.
- the molten metal may be discharged by said pump through pipe 20 into a reaction or mixing chamber 21.
- Chamber 21 may be provided with a series of baffle-plates 22,
- baffle-plates 22 should be such that the metal introduced from pipe 20 may flow in a comparatively thin film thereover.
- the metal After flowing over the various baflle-plates, the metal may be discharged into kettle 10 means of discharge pipe 23, which prefera ly extends a comparatively small distance below the surface of the metal contained therein whereby agitation of the metal is prevented.
- the required reagent may. be added to the metal in the reaction-chamber by any suit- Y able means,
- a reagent may be added to the metal during the refining process without causing agitation of the mass of metal or interfering with the formation of the dross on the surface thereof. Furthermore, a complete reaction may be had with each part of the metal, due to the intimatecontact obtained between the reagent and the metal itself, which ensures the eificient removal of the undesired substances without the use of an excessive quantity of reagent.
- the. rate of the reaction may be controlled practically independently of the total amount of metal present, and the quantity of reagent reimpurities may be determined by the rateof flow rather than by the total amount of metal present.
- Reaction-chamber 21 in Fig. 2 instead of being provided with a series of baffle-plates 22, contains an inverted cone 24, over the surface of which the metal discharged from pipe 20 is caused to flow and is mixed with the reagent which may be discharged from hopper 30.
- the reaction between the metal and the reagent is facilitated in this case by producing a thin film over the surface of inverted cone 24 and by allowing the metal to drop, in the form of.
- An apparatus for the refining of lead comprising a kettle adapted to contain the molten lead, a reaction-chamber, means for supporting said chamber on said kettle, a pump located in the lowerportion of said kettle and supported from said supporting means, said pump being adapted to withdraw metal from said kettle and to discharge the same in the said reaction-chamber, a series of inter-leaved bafile-plates in said chamber, the rate of discharge of said metal bein such that a thin filmof molten lead is forme over the surface of said plates, means for adding a reagent to said ,film, and means for collecting and discharging said metal and said reagent into said kettle.
- An apparatus for refining metals comprising, in combination, a container in which the metal is heated to molten state, a reaction chamber, means to withdraw molten metal from the container and discharge it to the reaction chamber, bafiie plates associated with the chamber to spread the molten metal into a film, means to add a' potentially reactive solid to the film, and means to discharge the metal from the reaction chamber to the container and below the liquid level therein.
- the rate of discharge of said metal being such that a thin film of molten lead is
Description
Oct. 29, 1929. w, YORK 1,733,522
APPARATUS FOR REFINING METALS Filed Feb. 9, 1927 Patented Oct. 29, 1929 UNITED STATES PATENT OFFICE HERBERT W. YORK, 01! NEW YORK, N. Y.,
ASSIGNOR TO AMERICAN SMELTING AND REFINING COMPANY, OF NEW YORK, N. Y., A CORPORATION OF NEW JERSEY APPARATUS FOR. REFINING METALS Application filed February 9, 1927. Serial No. 166,892.
This invention relates to metal refining, and, more particularly, to a method and apparatus for removing impurities from molten metals by the addition of a suitable reagent 5 thereto.
The invention relates more specifically to the refining of'metals by passing them, in a molten condition, over a suitable surface to form a thin film, and adding the reagent to said film.
The invention further consists in the new and novel features of operation and the new and original arrangementsand combinations of steps in the process hereinafter described and more particularly set forth in the claims.
In certain types of metallurgical processes, for examplein the refining of lead, it is desirable to remove impurities b the addition of a suitable reagent for uniting with the impurities to produce a compound which floats upon the surface of the molten metal as a dross. In lead refinin impurities such as copper may be remove as a dross by reacting the molten metal with sulphur under suitable conditions for causing the sulphur to readily unite with the copper content of the metal.
In accordance with the present invention, which will be described as applied to the removal of copper from lead by the addition of sulphur, although it is app icable generally to processes requiring the addition of a reagent to a fluid substance, the molten metal ,is caused to pass, in a com aratively thin film, over a suitable surface. he reagent may be added to the flowing film, which presents a large surface area per unit of mass, and, by reason of the thin film. may be brought into intimate contact with the various portions of the metal. It may be further mixed with the metal by causing agitation of the film before returning the same to the bath.
Although the novel features which are believed to e characteristic of this invention will be particularly pointed out in the claims appended hereto, the invention itself, as to its objects and advantages, the mode of its operation and the manner of its organization may be better understood by referring to the 50 following description taken in connection with the accompanying drawings forming a part thereof, in which Fig. 1 is a diagrammatic representation of one orm of apparatus which may be employed in carrying out this process; and,
Fig. 2 represents a modified form of mixing-chamber which may be employed therein.
Like. refcrencecharacters denote like parts in the several figures of the drawings.
In the following description and in the claims parts will be identified by specific names for convenience, but they are intended to be as generic in their application to similar parts as the art will permit.
' Referring to the figures more in detail, the material to be treated, such as molten lead, may be contained in a suitable kettle 10, which is adapted to be heated by a furnace or other means (not shown). Molten metal may be removed from kettle 10 by means of centrifugal pump 11, which is supported in the lower portion of said kettle from beam 11', extendmg across and resting upon the rim of said kettle. Pump 11 may be driven by motor 12, which is supported by and carried upon said beam, and is driven by means of rod 13 connecting said motor and said pump. Suitable bracin means 14 may be employed, if desired, For maintaining pump 11 in the desired position.
The molten metal may be discharged by said pump through pipe 20 into a reaction or mixing chamber 21. Chamber 21 may be provided with a series of baffle-plates 22,
which are inter-leaved in such manner that. metal, in flowing from pipe 20 over the various successive plates, falls from one plate to another and is agitated in so doing. The area of said baffle-plates 22 should be such that the metal introduced from pipe 20 may flow in a comparatively thin film thereover. After flowing over the various baflle-plates, the metal may be discharged into kettle 10 means of discharge pipe 23, which prefera ly extends a comparatively small distance below the surface of the metal contained therein whereby agitation of the metal is prevented.
The required reagent may. be added to the metal in the reaction-chamber by any suit- Y able means,
' quired for the removal of such as by hopper 30, the rate of said reagent being controlled 31 in the lower portion of addition by valve mechanism of said hopper.
By means of this process, a reagent may be added to the metal during the refining process without causing agitation of the mass of metal or interfering with the formation of the dross on the surface thereof. Furthermore, a complete reaction may be had with each part of the metal, due to the intimatecontact obtained between the reagent and the metal itself, which ensures the eificient removal of the undesired substances without the use of an excessive quantity of reagent.
By removing the metal in small quantities from the mass of metal present in the kettle and acting upon the small quantity removed independently of the remaimng portions, the. rate of the reaction may be controlled practically independently of the total amount of metal present, and the quantity of reagent reimpurities may be determined by the rateof flow rather than by the total amount of metal present.
By mixing the flowing stream of metal with I the reagent in the reaction-chamber, it is possible to obtain a much more intimate contact between the various elements than would be possible by introducing the reagent into the mass oi molten metal itself. Furthermore, should the reagent be introduced directly into the molten metal, it would be necessary to provide suitable means for agitation in order to cause a complete reaction over the entire mass. 7
-In Fig. 2, the various parts corresponding to parts shown in Fig. 1 are given corresponding reference numbers. Reaction-chamber 21 in Fig. 2, however, instead of being provided with a series of baffle-plates 22, contains an inverted cone 24, over the surface of which the metal discharged from pipe 20 is caused to flow and is mixed with the reagent which may be discharged from hopper 30. The reaction between the metal and the reagent is facilitated in this case by producing a thin film over the surface of inverted cone 24 and by allowing the metal to drop, in the form of.
a comparatively fine spray, from the edges of said cone\ to the lower part'of reaction-tank 21. The action of the various elements when passed through the apparatus shown in Fig.
' 2 will be similar to that described in connecstood that the structure may be modified in various respects without departure from the greases same in the said reaction-chamber, and a series of inter-leaved bafiie-plates in said chamber,
formed over the surface of said plates. .2. An apparatus for the refining of lead comprising a kettle adapted to contain the molten lead, a reaction-chamber, means for supporting said chamber on said kettle, a pump located in the lowerportion of said kettle and supported from said supporting means, said pump being adapted to withdraw metal from said kettle and to discharge the same in the said reaction-chamber, a series of inter-leaved bafile-plates in said chamber, the rate of discharge of said metal bein such that a thin filmof molten lead is forme over the surface of said plates, means for adding a reagent to said ,film, and means for collecting and discharging said metal and said reagent into said kettle.
An apparatus for refining metals, com prising, in combination, a container in which the metal is heated to the molten condition, means to continuously withdraw a stream of the molten metal from the container, a reaction chamber, baflle construction associated with the reaction chamber to convert the stream of molten metal into a relatively thin film and means to add a potentially reactive solid to the film of metal.
4. An apparatus for refining metals comprising, in combination, a container in which the metal is heated to molten state, a reaction chamber, means to withdraw molten metal from the container and discharge it to the reaction chamber, bafiie plates associated with the chamber to spread the molten metal into a film, means to add a' potentially reactive solid to the film, and means to discharge the metal from the reaction chamber to the container and below the liquid level therein.
In testimony whereof I have hereunto set my hand and seal.
HERBERT W. YORK.
the rate of discharge of said metal being such that a thin film of molten lead is
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US166892A US1733522A (en) | 1927-02-09 | 1927-02-09 | Apparatus for refining metals |
Applications Claiming Priority (1)
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US166892A US1733522A (en) | 1927-02-09 | 1927-02-09 | Apparatus for refining metals |
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US1733522A true US1733522A (en) | 1929-10-29 |
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US166892A Expired - Lifetime US1733522A (en) | 1927-02-09 | 1927-02-09 | Apparatus for refining metals |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2528209A (en) * | 1946-07-12 | 1950-10-31 | Walter M Weil | Apparatus for smelting metals |
US2528208A (en) * | 1946-07-12 | 1950-10-31 | Walter M Weil | Process of smelting metals |
-
1927
- 1927-02-09 US US166892A patent/US1733522A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2528209A (en) * | 1946-07-12 | 1950-10-31 | Walter M Weil | Apparatus for smelting metals |
US2528208A (en) * | 1946-07-12 | 1950-10-31 | Walter M Weil | Process of smelting metals |
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