US572312A - Electric furnace - Google Patents
Electric furnace Download PDFInfo
- Publication number
- US572312A US572312A US572312DA US572312A US 572312 A US572312 A US 572312A US 572312D A US572312D A US 572312DA US 572312 A US572312 A US 572312A
- Authority
- US
- United States
- Prior art keywords
- electrodes
- furnace
- hearth
- electrode
- hopper
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 239000000463 material Substances 0.000 description 47
- 239000007789 gas Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 239000004020 conductor Substances 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 206010022000 influenza Diseases 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000000284 resting effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/18—Charging particulate material using a fluid carrier
Definitions
- the object of this invention is to decompose the ore or other material or melt the same under the electrical operation and to cause the melted or decomposed material to run 011: the hearth or bottom of the furnace as such materials are melted.
- the electrodes can be sufficiently near to each other to act to the best advantage and so that such elec trodes will not be immersed in the melted or changed material, and I so arrange the parts of this furnace that the operations may be substantially continuous.
- I provide the furnace with a straight or nearly straight bottom and with inclosing sides sufficient-ly deep to hold the required amount of material, and the furnace is pivotally supported and constructed in such a manner that it may be tipped more or less to give greater or less inclination to the bottom of the furnace along which the melted or changed material passes to the place of delivery, and the electrodes, which are preferably of carbon, are surrounded with cases, there being spaces between the electrodes and the cases for the pulverulent material to pass down to the point of fusion and the gases escape around the cases, and it is advantageous to make these cases hollow and to circulate water or similar material through the same, so as to convey away surplus heat and prevent the upper part of the electrodes becoming too highly heated.
- Figure 1 is a longitudinal vertical section.
- Fig. 2 is a cross-section at a; :20, Fig. 1, through the smelting portion of the furnace.
- Fig. 3 is a cross-section at y 3 Fig. 1, showing the mechanism for supporting the furnace and varying the inclination of the bottom or hearth; and
- Fig. 4 is a sectional plan at the line ,2 a, Fig. 1.
- the furnace is made with side walls 4, resting upon a bottom plate 1, and there is a hearth or bottom 2, preferably of carbon, in the form of a slab, and it is usually advantageous to employ slabs of carbon at the sides of the furnace, as shown at 3, and upon the upper portions of the walls 4 a suitable bin or hopper 30 is provided, and I remark that the size and shape of the furnace-walls and the hopper may vary according to the character of the material to be operated upon, and the number of the electrodes may also vary according to the size of the furnace.
- electrodes 5 which are advantageously of carbon and placed vertically, and each electrode is provided with a holder or clip 16, that permanently connects the carbon electrode to the conductor, which is advantageously formed of a rod 19, screwthreaded and passing through the supports 21 upon a beam 28, there being a hand-wheel and nut 20 by which to raise or lower the electrode to bring the lower end of such electrode into proper proximity to the hearth or floor 2 of the furnace, and I remark that the conductors from the dynamo are to be connected to the heads 49 of the rods 19 in any desired manner, and by channeling the rods 19 longitudinally and providing the guides 22 with projecting keys entering such slots the screws 19 are held from rotating by the action of the hand-wheels and nuts 20.
- the furnace bottom plate 1 is pivoted to a suitable support.
- back end of the furnace can be raised or lowered bodily by the nuts on the screw-rod 46, so as to incline the bottom of the furnace to a greater or less extent to cause the melted material to flow with suiiicient freedom to run oif the hearth or bottom of the furnace into a suitable receptacle 10, which receptacle 10 can be pressed tightly up against the under side of the plate 1 by a wedge 29 or other suitable device, so as to exclude atmosphere as far as possible.
- the material to be acted upon is introduced in a pulverulent condition into the hopper 30, and it settles down around the electrodes 5 and rests upon the hearth or bottom 2 of the furnace, and I find it advantageous to make use of the hollow cases 6, which surround the electrodes adjacent to the bottom and inner edges of the hopper, and these hollow cases 6 are advantageously kept cool by water circulating through the same from the pipe 31, the discharge being through the pipes 33, and between these cases 6 and electrodes 5 there are spaces sufficient for the pulverulent material to subside around the electrodes, and the upper parts of the cases (3 are connected together, as shown in Fig.
- the pulverulent materials will be subject to the action of the electric are between the electrodes 5 and the hearth or bottom 2 of the furnace, and such materials will be melted or decomposed by the electric action or recombined, according to the character of the materials under treatment, and that the metal or other material that is fused or reduced upon the hearth 2 will run along such hearth in consequence of the inclination until it finally escapes from the end of the hearth into the receptacle 10, and there is ample opportunity for gases to escape by the dues 7, and the materials within the hopper are kept in a comparatively cool condition until they pass by the cases (3.
- the furnace is capable of extension substantially indefinitely, so that its capacity may be increased, and the electric arcs are constantly acting upon fresh untreated material as the changed material passes off the hearth. Either electrode can be replaced when so desired without necessarily arresting the action of the others.
- This furnace is adapted to the reduction of refractory metallic and non-metallic oxids and alloys of the same and for the production of metallic and alkaline earthy cal-bids by electric smelting and for other purposes in electric smelting, and by keeping the casings full of the material to be acted upon the atmosphcre is excluded as much as possible from the electrodes to prevent them from burning away, and at the same time the gases resulting from the reduction of the materials under treatment, together with such portions of the compounds as may escape, pass by the fines to the condensing or depositing chamber ll for the collection or condensation, or both, of such materials, and the vent-pipe or chimney allows for the escape of surplus gases.
- the operations performed in this furnace may be substantially continuous to avoid the expense of stopping and starting the furnace, because the materials can be supplied and the hopper kept sufiiciently full for such materials to descend by gravity, and it is ad vantageous to employan ammeter in the circuit to each of the electrodes, so that a uniform or nearly uniform current can be passed through each electrode, the regulation of the current being effected by raising or lowering the electrode and thereby increasing or decreasing the resistance, and the furnace can be kept in operation until the electrodes are consumed or nearly so.
- the electrodes should be substantially vertical; but the entire furnace can be swung upon its pivot to any desired inclination, or constructed with the electrodes at any desired inclination, or even horizontal or nearly so, according to the material acted upon, without substantially departing from the subjectmatter of the present invention.
- the conductors of opposite polarity to those that are connected to the electrodes 5 are connected to the bottom plate 1, as at 42.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
3 Sheets8heet 1.
(No Model.) E. P. PRICE ELECTRIC FURNACE.
Patented Dec. 1, 18 96.
m: Noam: PETERS cov wow-Limo wnnmamm a c (No Model.) 3 Sheets-Sheet 2 E. F. PRICE. ELECTRIC FURNACE.
Patented Dec. 1, 1896.
m: mums warms co, PNOTO-LITHO, wasnwnmu, n:v c.
UNITED STATES PATENT OFFICE.
EDGAR F. PRICE, OF NElVARK, NElV JERSEY.
ELECTRIC FURNACE.
SPECIFICATION forming part of Letters Patent No. 572,312, dated December 1, 1896.
Application filed July 22, 1895. Renewed April 11, 1896. Serial No. 587,233. (No model.)
To (all 1072,0172, it may concern,-
Be it known that I, EDGAR F. PRICE, a citizen of the United States, residing at Newark, in the county of Essex and State of New Jersey, have invented an Improvement in Electric Furnaces, of which the following is a specification.
The object of this invention is to decompose the ore or other material or melt the same under the electrical operation and to cause the melted or decomposed material to run 011: the hearth or bottom of the furnace as such materials are melted. Hence the electrodes can be sufficiently near to each other to act to the best advantage and so that such elec trodes will not be immersed in the melted or changed material, and I so arrange the parts of this furnace that the operations may be substantially continuous.
I provide the furnace with a straight or nearly straight bottom and with inclosing sides sufficient-ly deep to hold the required amount of material, and the furnace is pivotally supported and constructed in such a manner that it may be tipped more or less to give greater or less inclination to the bottom of the furnace along which the melted or changed material passes to the place of delivery, and the electrodes, which are preferably of carbon, are surrounded with cases, there being spaces between the electrodes and the cases for the pulverulent material to pass down to the point of fusion and the gases escape around the cases, and it is advantageous to make these cases hollow and to circulate water or similar material through the same, so as to convey away surplus heat and prevent the upper part of the electrodes becoming too highly heated.
In the drawings, Figure 1 is a longitudinal vertical section. Fig. 2 is a cross-section at a; :20, Fig. 1, through the smelting portion of the furnace. Fig. 3 is a cross-section at y 3 Fig. 1, showing the mechanism for supporting the furnace and varying the inclination of the bottom or hearth; and Fig. 4 is a sectional plan at the line ,2 a, Fig. 1.
The furnace is made with side walls 4, resting upon a bottom plate 1, and there is a hearth or bottom 2, preferably of carbon, in the form of a slab, and it is usually advantageous to employ slabs of carbon at the sides of the furnace, as shown at 3, and upon the upper portions of the walls 4 a suitable bin or hopper 30 is provided, and I remark that the size and shape of the furnace-walls and the hopper may vary according to the character of the material to be operated upon, and the number of the electrodes may also vary according to the size of the furnace.
I have shown electrodes 5, which are advantageously of carbon and placed vertically, and each electrode is provided with a holder or clip 16, that permanently connects the carbon electrode to the conductor, which is advantageously formed of a rod 19, screwthreaded and passing through the supports 21 upon a beam 28, there being a hand-wheel and nut 20 by which to raise or lower the electrode to bring the lower end of such electrode into proper proximity to the hearth or floor 2 of the furnace, and I remark that the conductors from the dynamo are to be connected to the heads 49 of the rods 19 in any desired manner, and by channeling the rods 19 longitudinally and providing the guides 22 with projecting keys entering such slots the screws 19 are held from rotating by the action of the hand-wheels and nuts 20.
The furnace bottom plate 1 is pivoted to a suitable support. I have represented the pivotal bar 36 as passing through lugs upon the bottom plate 1, such bar 36 resting upon suitable bearings 34 upona foundation or supports 35, and the beam 28 should be connected with the furnace by the slings or rods 41, that pass through the lugs 25, that project from the bottom plate 1, and are connected thereto by suitable nuts, and these rods 41 pass up in the form of a yoke to the beam 28, and by means of an eye 27, yoke, and screw-rod 46, through a beam or permanent support, the
back end of the furnace can be raised or lowered bodily by the nuts on the screw-rod 46, so as to incline the bottom of the furnace to a greater or less extent to cause the melted material to flow with suiiicient freedom to run oif the hearth or bottom of the furnace into a suitable receptacle 10, which receptacle 10 can be pressed tightly up against the under side of the plate 1 by a wedge 29 or other suitable device, so as to exclude atmosphere as far as possible.
It will be understood that the material to be acted upon, as shown at A, is introduced in a pulverulent condition into the hopper 30, and it settles down around the electrodes 5 and rests upon the hearth or bottom 2 of the furnace, and I find it advantageous to make use of the hollow cases 6, which surround the electrodes adjacent to the bottom and inner edges of the hopper, and these hollow cases 6 are advantageously kept cool by water circulating through the same from the pipe 31, the discharge being through the pipes 33, and between these cases 6 and electrodes 5 there are spaces sufficient for the pulverulent material to subside around the electrodes, and the upper parts of the cases (3 are connected together, as shown in Fig. 1, so that there are spaces 7 between one case and the next, which spaces form fines for the gases or other volatile materials to pass away, and these spaces '7 open into longitudinal flues 17, leading to any suitable chamber in which useful by-products maybe condensed, or such vapors may pass to a chimney 13. It will now be understood that the pulverulent materials will be subject to the action of the electric are between the electrodes 5 and the hearth or bottom 2 of the furnace, and such materials will be melted or decomposed by the electric action or recombined, according to the character of the materials under treatment, and that the metal or other material that is fused or reduced upon the hearth 2 will run along such hearth in consequence of the inclination until it finally escapes from the end of the hearth into the receptacle 10, and there is ample opportunity for gases to escape by the dues 7, and the materials within the hopper are kept in a comparatively cool condition until they pass by the cases (3. Hence but a small quantity of the material is .under treatment at one time, but the furnace is capable of extension substantially indefinitely, so that its capacity may be increased, and the electric arcs are constantly acting upon fresh untreated material as the changed material passes off the hearth. Either electrode can be replaced when so desired without necessarily arresting the action of the others.
This furnace is adapted to the reduction of refractory metallic and non-metallic oxids and alloys of the same and for the production of metallic and alkaline earthy cal-bids by electric smelting and for other purposes in electric smelting, and by keeping the casings full of the material to be acted upon the atmosphcre is excluded as much as possible from the electrodes to prevent them from burning away, and at the same time the gases resulting from the reduction of the materials under treatment, together with such portions of the compounds as may escape, pass by the fines to the condensing or depositing chamber ll for the collection or condensation, or both, of such materials, and the vent-pipe or chimney allows for the escape of surplus gases.
The operations performed in this furnace may be substantially continuous to avoid the expense of stopping and starting the furnace, because the materials can be supplied and the hopper kept sufiiciently full for such materials to descend by gravity, and it is ad vantageous to employan ammeter in the circuit to each of the electrodes, so that a uniform or nearly uniform current can be passed through each electrode, the regulation of the current being effected by raising or lowering the electrode and thereby increasing or decreasing the resistance, and the furnace can be kept in operation until the electrodes are consumed or nearly so.
It will be apparent that in order to avail of gravity in feeding the materials from the hopper the electrodes should be substantially vertical; but the entire furnace can be swung upon its pivot to any desired inclination, or constructed with the electrodes at any desired inclination, or even horizontal or nearly so, according to the material acted upon, without substantially departing from the subjectmatter of the present invention. The conductors of opposite polarity to those that are connected to the electrodes 5 are connected to the bottom plate 1, as at 42.
It will be seen in Fig. 1 that the end electrode in the range is closely adjacent to the edge of the hearth over which the material is delivered, and there is not any material fed around such electrode. Hence the material passing from around the other electrodes cannot escape from the edge of the inclined hearth without passing closely adjacent to this electrode, so as to be acted upon and brought into the proper condition before running off to the receptacle 10.
I claim as my inventionl. The combination in a furnace of a conducting-hearth forming one electrode, a range of electrodes substantially perpendicular to the hearth and means for adjusting the electrodes and regulating the currents, a supplyhopper for the material to pass down around the electrodes, and means for varying the inclination of the hearth and the movement of the material thereon as it passes from one electrode to another substantially as specified.
2. The combination with a furnace having an inclined bottom or hearth, of a range of electrodes substantially perpendicular to such bottom, means for supporting and adj usting the electrodes toward or from the hearth and means for supplying the material to be acted upon around such electrodes, and casings around the electrodes, there being spaces between such casing and the electrodes for the passage of the material acted upon, substantially as set forth.
3. The combination with a furnace having be acted upon around such electrodes, a 1101 low casing around each electrode and means for supplying a circulating fluid through such hollow casings to regulate the temperature thereof, there being spaces between the electrodes and the casings for the passage of the material to be acted upon, substantially as set forth.
4. The combination with an inclined hearth of a range of electrodes over such hearth and electric connections to the hearth and to the electrodes and means for supplying the material to be treated around the electrodes in the range, except the one adjacent to the place of delivery from the hearth, so that the materials cannot pass off the hearth without being subjected to the electric operation, substantially as specified.
5. The combination in an electric furnace, of a hearth or bottom forming one electrode, a range of electrodes substantially perpendicular to the bottom, casings around the respective electrodes and a hopper With which such casings are connected, there being spaces between the casings and the electrodes for the passage of the material acted upon, substantially as specified.
6. The combination in an electric furnace, of a hearth or bottom forming one electrode, a range of electrodes substantially perpendicular to the bottom, casings around the respective electrodes and a hopper with which such casings are connected, there being spaces between the casings and the electrodes for the passage of the material acted upon, the easings being provided with openings forming flues, and fines into which the escaping gases or other materials pass and a chamber to which they are led, substantially as set forth.
7. The combination in an electric furnace,
of a hearth or bottom forming one electrode, a range of electrodes substantially perpendicular to the bottom, casings around the respective electrodes and a hopper with which such casings are connected, there being spaces between the casings and the electrodes for the passage of the material acted upon, a pivotal support for the furnace and means for adj usting the inclination of the bottom or hearth, substantially as set forth.
8. The combination in an electric furnace, of a bottom or hearth, a pivoted plate for supporting the same, side walls and a hopper for the material to be acted upon, an electrode and means for adjusting the proximity of the end of the same to the bottom of the hearth, a casing surrounding the electrode, there being a space between the casing and the electrode for the material in the hopper to pass down to the hearth, supporting-rods and a screw for adjusting the furnace upon its pivotal support and varying the inclination of the hearth, and a removable pot for receiving the product from the furnace, substantially as set forth.
9. The combination in an electric furnace with a conductor forming the furnace-hearth from which the changed material is allowed to pass off by gravity, of an adjustable electrode above the hearth, a supply-hopper from which the material to be treated descends around the upper electrode and a lateral escape for the gases to prevent them ascending through the material under treatment, substantially as specified.
Signed by me this 17th day of July, 1895.
EDGAR F. PRICE.
Witnesses:
GEO. T. PINCKNEY, S. T. HAVILAND.
Publications (1)
Publication Number | Publication Date |
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US572312A true US572312A (en) | 1896-12-01 |
Family
ID=2641010
Family Applications (1)
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US572312D Expired - Lifetime US572312A (en) | Electric furnace |
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US (1) | US572312A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2648714A (en) * | 1950-04-01 | 1953-08-11 | American Cyanamid Co | Hood for electric furnace |
US2671124A (en) * | 1951-05-24 | 1954-03-02 | Union Carbide & Carbon Corp | Electric reduction furnace |
US2896108A (en) * | 1957-01-31 | 1959-07-21 | Stanley M Segal | Apparatus employing horizontally elongated carbon arc sources |
US3783169A (en) * | 1972-09-05 | 1974-01-01 | Koppers Co Inc | Method and apparatus for the continuous fluidizing of steel |
-
0
- US US572312D patent/US572312A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2648714A (en) * | 1950-04-01 | 1953-08-11 | American Cyanamid Co | Hood for electric furnace |
US2671124A (en) * | 1951-05-24 | 1954-03-02 | Union Carbide & Carbon Corp | Electric reduction furnace |
US2896108A (en) * | 1957-01-31 | 1959-07-21 | Stanley M Segal | Apparatus employing horizontally elongated carbon arc sources |
US3783169A (en) * | 1972-09-05 | 1974-01-01 | Koppers Co Inc | Method and apparatus for the continuous fluidizing of steel |
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