US409489A - Kiln for the manufacture of carbons - Google Patents
Kiln for the manufacture of carbons Download PDFInfo
- Publication number
- US409489A US409489A US409489DA US409489A US 409489 A US409489 A US 409489A US 409489D A US409489D A US 409489DA US 409489 A US409489 A US 409489A
- Authority
- US
- United States
- Prior art keywords
- chamber
- carbons
- furnace
- conveyers
- kiln
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title description 10
- 238000002485 combustion reaction Methods 0.000 description 12
- 239000007789 gas Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 239000000446 fuel Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000011819 refractory material Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000001105 regulatory Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 102100017923 ACOT12 Human genes 0.000 description 2
- 101710008266 ACOT12 Proteins 0.000 description 2
- 240000001973 Ficus microcarpa Species 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 230000001737 promoting Effects 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
- F27B9/14—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
- F27B9/20—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace
- F27B9/26—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace on or in trucks, sleds, or containers
- F27B9/262—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace on or in trucks, sleds, or containers on or in trucks
Definitions
- PETERS PhowLnhngnplmr. wnshmgmn. uc.
- My invention relates to the manufacture of carbon electrodes as used in arc lamps for electric lighting; but I do not desire to limit the invention in this particular, though it is particularly adapted for this purpose.
- the invention comprises a long heating or carbonizin g chamber in connection With a furnace at one end or heating-chamber, and with a suitable flue or outlets with valves for controlling ihe draft, and thus regulating the temperature of the carbonizing-chamber; of conveyers Within the chamber and recepta- .cles for the caibons to be treated mounted upon or formed with the conveyers; means for cooling the conveyers; means for promoting the combustion of the gases arising' from the receptacle containing the carbons under treatment, and, finally, many details of construction Which I will describe more particularly hereinafter.
- Figure l represents a side elevation of the complete furnace; Fig. 2, a longitudinal vertical section.
- Fig. 3 is a longitudinal section taken horizontally on the line F G of Fig. l.
- Fig. 4 is an end elevation of Fig. l, While Fig. 5 shows an end elevation of the furnace end.
- Fig. G is a section through the, line B C of Fig. 2.
- Fig. 7 is a section through the lineC D of Fig. 2.
- Fig. S is a detail View of thc con veyer in inverted position.
- the furnace proper is shown at A, and it consists of ordinary gratebars with an ash-pit beneath and doors a a leading thereto, with doors e' leading to the opening above the grate-bars.
- a bridge-Wall J which forms a contracted opening from the iirechamber to an elongated chamber B, in which the carbons are baked.
- Both' the fire-chamber and the bakingchamber are preferably built of brick-work suitably braced by iron-Work, as shown in the drawings.
- a long baking-chamber is preferably formed on an inclined plane 5 5 from the firing-chamber upward to the opposite end, Where the carbons in their green state are inserted preparatory to being subjected to the baking process.
- sliding doors U are provided, which, preferably, have means for opening them upward to admit the receptacles containing the carbons.
- the bottom floor of the baking-chalnber is made inclined, so as to aid in the movement of the receptacles in their passage through the chamber from one end to the other.
- I provide an underground flue from the baking-chamber leading to a suitable chimney, and I prefer to have openings leading to this flue from the chamber B at different points, as shown at A B C', providing each opening With a suitable valve, as shown at G II I', and more or less of these openings may be provided, the purpose being to provide means by Which the temperature of the chamber B may be regulated with absolute certainty at different points in its extent, as it is necessary that the temperature shall vary Within the chamber, being greatest in that part nearest the fire-chamber and growing less gradually and uniformly toward the opposite end, so that the action upon the carbons is regular, beginning with a drying heat and finally reaching a White heat to complete the baking process.
- Extending along the bottom of the bakingchamber is a series of tracks S, which are ai 95 IOO of the conveyers being formed inclined, their upper faces are in horizontal plane, and are thus adapted to hold the receptacles which contain the carbons (indicated at WV) in an upright position.
- These conveyers are preferably made of refractory material, so as to withstand the excessive heat to which they are subjected, and as shown I make them separate from the conveyers themselves. I may, however, form the conveyers and receptacles in onepiece; but I prefer making them independent of each other, as they can thus be more readily handled.
- I connect the ends of the pipes S at the upper end of the chamber B with a suitable water-supply, and in this manner provide a constant ilow of water through the pipe, which tends to lower the temperature where contact is made with the groove of the conveyer and permits of a lubricant being used to facilitate the descent of the conveyers with their load.
- the lower ends of the pipes S are in connection with the ash-box by means of a pipe b', and as the water is converted into steam it is discharged in the form of very dry steam beneath the grate, where it aids in the combustion of the fuel and tends t0 economize in the amount of fuel necessary to run the furnace.
- the carbons are placed in suitable receptacles W, which are mounted upon the conveye'rs G so as to have a space all around each receptacle, and thus allow the heat to attack and penetrate from all sides of each receptacle, and thus allowing also a more uniform heating. It will be seen that the heat passes above the conveyers and the carbons are subjected to la uniform and gradual heating, beginning at their upper ends and continuing to the bottom. As the receptacles are kept in a vertical position, the carbons pass through the furnace without being changed from the vertical position, and thus they are kept straight, and there is no liability of their becoming bent or breaking. At different positions I place pyrometers to indicate the temperature of the furnace at different stages of the process.
- the temperature in the grate or fire-place is maintained at a comparatively uniform high heat, and the furnace from the fire-bridge to perhaps twenty feet, or about one-third the extent of the furnace, is kept at a white heat, and from this point to the upper end of the furnace the temperature gradually diminishes until where it reaches the doors U it is quite low, as the carbon cases and conveyers absorb a great deal of the heat.
- I provide doors-such as F G I'I-at intervals in the extent of the furnace, as shown in Fig. l, and through these doors the interior of the furnace may be reached, and at the last door F the cases containing the carbons may be removed in any suitable manner and by suitable means.
- atruck is inserted which comes to a level with the top of the conveyer, and the receptacle W is drawn off onto the truck and thus removed.
- the series of conveyers may be aided in their movement through the furnace by any suitable means, such as the hydraulic jack represented at R in Fig. l.
- a heating-chamber having tubular tracks laid in the bottom thereof, conveyers adapted to said track, a suitable watersupply, in connection with said tubular track, and apipe-connection between the lower end of the track and the ash-pit of the fire-chamber, substantially as described.
- a series of independent sliding conveyers composed of refractory material and receptacles for the carbons mounted upon said conveyers and moving therewith, substantially as described.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Tunnel Furnaces (AREA)
Description
2 Sheets-Sheet 1.
(No Model.) l
P. P. NUNGESSER.
KILN POR THE MANUFAGTURE 0F ARBONS.
No. 409,489. e Patented Aug. 20, 1889.
IIIIIIIII Y I v WWA | l l l I N. Firms. Phow-Liuwgmpher. wnsningmn. u. c.
2 Sheets-Sheet 2.
Patented Aug. 20, 1889.
N. PETERS PhowLnhngnplmr. wnshmgmn. uc.
P. P. NUNGESS'ER.
(No Model.)
KILN POR THE MANUPAGTURE OP GARBONS.
ps Y i X *v H M. I \L[ u I m f w Nn N \w/v u||||| n u |||||||||Hn m 1111111H1111111121111 ll 1111111v lu. 1 111 11111113 111 11 1 HI 1.- wm h.
UNITED STATES PATENT OEEICE.
PHILIP P. NUNGESSER, OF CLEVELAND, OHIO.
KILN FOR THE IVIANUFACTURE OF CARBONS.
SPECIFICATION forming part of Letters Patent No. 409,489, dated August 20, 1889.
Application filed December 27, 1888. Serial No. 294,790. (No model.)
T0 all whom it may concern-.-
Be it known that I, PHILIP P. NUNGESSER, of Cleveland, in the county of Cuyahoga and State of Ohio, have invented a new and useful Improvement in the hilanufacture of Carbons; and I do hereby declare that the following is afull, clear, and exact description of the same.
My invention relates to the manufacture of carbon electrodes as used in arc lamps for electric lighting; but I do not desire to limit the invention in this particular, though it is particularly adapted for this purpose.
The invention comprises a long heating or carbonizin g chamber in connection With a furnace at one end or heating-chamber, and with a suitable flue or outlets with valves for controlling ihe draft, and thus regulating the temperature of the carbonizing-chamber; of conveyers Within the chamber and recepta- .cles for the caibons to be treated mounted upon or formed with the conveyers; means for cooling the conveyers; means for promoting the combustion of the gases arising' from the receptacle containing the carbons under treatment, and, finally, many details of construction Which I will describe more particularly hereinafter. i
It- Will be understood that the invention consists in the parts enumerated above, combined as pointed out in the claims.
In the accompanyingr drawings, Figure l represents a side elevation of the complete furnace; Fig. 2, a longitudinal vertical section. Fig. 3 is a longitudinal section taken horizontally on the line F G of Fig. l. Fig. 4 is an end elevation of Fig. l, While Fig. 5 shows an end elevation of the furnace end. Fig. G is a section through the, line B C of Fig. 2. Fig. 7 is a section through the lineC D of Fig. 2. Fig. S is a detail View of thc con veyer in inverted position.
In the drawings, the furnace proper is shown at A, and it consists of ordinary gratebars with an ash-pit beneath and doors a a leading thereto, with doors e' leading to the opening above the grate-bars. In rear of the grate-bars is a bridge-Wall J, which forms a contracted opening from the iirechamber to an elongated chamber B, in which the carbons are baked. Both' the fire-chamber and the bakingchamber are preferably built of brick-work suitably braced by iron-Work, as shown in the drawings. A long baking-chamber is preferably formed on an inclined plane 5 5 from the firing-chamber upward to the opposite end, Where the carbons in their green state are inserted preparatory to being subjected to the baking process. At this end sliding doors U are provided, which, preferably, have means for opening them upward to admit the receptacles containing the carbons. The bottom floor of the baking-chalnber is made inclined, so as to aid in the movement of the receptacles in their passage through the chamber from one end to the other.
I provide an underground flue from the baking-chamber leading to a suitable chimney, and I prefer to have openings leading to this flue from the chamber B at different points, as shown at A B C', providing each opening With a suitable valve, as shown at G II I', and more or less of these openings may be provided, the purpose being to provide means by Which the temperature of the chamber B may be regulated with absolute certainty at different points in its extent, as it is necessary that the temperature shall vary Within the chamber, being greatest in that part nearest the fire-chamber and growing less gradually and uniformly toward the opposite end, so that the action upon the carbons is regular, beginning with a drying heat and finally reaching a White heat to complete the baking process.
I do not limit myself to the underground flue in connection at several points with the baking-chamber, as it Will be understood that chimneys may be erected instead, cach being` in connection with the chamber and controlled` 9o by suitable valves, Which would thus have the same effect; but I prefer the arrangement shown as bein-g more economical.
Extending along the bottom of the bakingchamber is a series of tracks S, which are ai 95 IOO of the conveyers being formed inclined, their upper faces are in horizontal plane, and are thus adapted to hold the receptacles which contain the carbons (indicated at WV) in an upright position. These conveyers are preferably made of refractory material, so as to withstand the excessive heat to which they are subjected, and as shown I make them separate from the conveyers themselves. I may, however, form the conveyers and receptacles in onepiece; but I prefer making them independent of each other, as they can thus be more readily handled. I connect the ends of the pipes S at the upper end of the chamber B with a suitable water-supply, and in this manner provide a constant ilow of water through the pipe, which tends to lower the temperature where contact is made with the groove of the conveyer and permits of a lubricant being used to facilitate the descent of the conveyers with their load. The lower ends of the pipes S are in connection with the ash-box by means of a pipe b', and as the water is converted into steam it is discharged in the form of very dry steam beneath the grate, where it aids in the combustion of the fuel and tends t0 economize in the amount of fuel necessary to run the furnace.
The carbons are placed in suitable receptacles W, which are mounted upon the conveye'rs G so as to have a space all around each receptacle, and thus allow the heat to attack and penetrate from all sides of each receptacle, and thus allowing also a more uniform heating. It will be seen that the heat passes above the conveyers and the carbons are subjected to la uniform and gradual heating, beginning at their upper ends and continuing to the bottom. As the receptacles are kept in a vertical position, the carbons pass through the furnace without being changed from the vertical position, and thus they are kept straight, and there is no liability of their becoming bent or breaking. At different positions I place pyrometers to indicate the temperature of the furnace at different stages of the process.
In practical operation the temperature in the grate or lire-place is maintained at a comparatively uniform high heat, and the furnace from the fire-bridge to perhaps twenty feet, or about one-third the extent of the furnace, is kept at a white heat, and from this point to the upper end of the furnace the temperature gradually diminishes until where it reaches the doors U it is quite low, as the carbon cases and conveyers absorb a great deal of the heat.
Y I have found in practice that it is necessary to provide for the combustion of the gases which are continually being expelled from the receptacles containing the carbons, or else a great deal of combustible matter would be wasted which might be utilized to increase the heating capacity of the furnace, and thus economize in the tonsumption of fuel. In order to obtain this combustion and to utilize these gases, I make the walls of the lire-chamber hollow, with passages extending to the front covered by suitable valves Y, and to the rear to the upper part of the bridge-wall, so that the heated air may pass out of the top of the arch, and, together with the superheated steam, form a perfect combustion at this point, which will also promote the combustion of the gases and vapors arising from the carbons under treatment, as above explained.
I provide doors-such as F G I'I-at intervals in the extent of the furnace, as shown in Fig. l, and through these doors the interior of the furnace may be reached, and at the last door F the cases containing the carbons may be removed in any suitable manner and by suitable means. Ordinarily atruck is inserted which comes to a level with the top of the conveyer, and the receptacle W is drawn off onto the truck and thus removed.
The series of conveyers may be aided in their movement through the furnace by any suitable means, such as the hydraulic jack represented at R in Fig. l.
The method of manufacturing carbons referred to herein, but not claimed, is the subject of a separate application filed in the United States Patent Office on the 31st of January, 1889, Serial No. 298,255.
I-laving thus described my invention, what I claim is v l. In the manufacture of carbons, a furnace having a fire-chamber at one end, an elongated heating-chamber in connection with the said fire-chamber, and a series of ilues controlled by suitable valves in connection with IOO said heating-chambers, substantially as de- Y scribed.
2. In the manufacture of carbons, afurnace the heating-chamber between the charging end and the fire-chamber, substantially as described.
3. In combination with a furnace having a fire-chamber, a heating-chamber having tubular tracks laid in the bottom thereof, conveyers adapted to said track, a suitable watersupply, in connection with said tubular track, and apipe-connection between the lower end of the track and the ash-pit of the fire-chamber, substantially as described.
4. In combination with a fire-chamber and a heating-chamber, a series of independent sliding conveyers composed of refractory material and receptacles for the carbons mounted upon said conveyers and moving therewith, substantially as described.
5. In combination, in the described furnace, with the tubular water-tracks, of independent sliding conveyers having grooves in their bottom adapted to said track and composed IIO of refractory material, substantially as de- 1o and the receptacles supported on said conveyers and of less Width, whereby spaces are provided between each receptacle, substantially as described.
In testimony whereof I have signed my naine to this speciication, in the presence of two sub- I 5 Scribing` Witnesses.
PHILIP P. NUN GESSER. 'Vitnesses:
G. C. METCALF, H. P. M oIw'rosH
Publications (1)
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US409489A true US409489A (en) | 1889-08-20 |
Family
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US409489D Expired - Lifetime US409489A (en) | Kiln for the manufacture of carbons |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2519250A (en) * | 1947-05-10 | 1950-08-15 | Norton Co | Tunnel kiln |
US2523025A (en) * | 1947-05-10 | 1950-09-19 | Norton Co | Tunnel kiln charging and discharging means |
US2618671A (en) * | 1948-12-28 | 1952-11-18 | Norton Co | Tunnel kiln |
US3183573A (en) * | 1960-07-26 | 1965-05-18 | Nat Tile & Mfg Co | Apparatus for making ceramic bodies and ceramic composition for use therewith |
-
0
- US US409489D patent/US409489A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2519250A (en) * | 1947-05-10 | 1950-08-15 | Norton Co | Tunnel kiln |
US2523025A (en) * | 1947-05-10 | 1950-09-19 | Norton Co | Tunnel kiln charging and discharging means |
US2618671A (en) * | 1948-12-28 | 1952-11-18 | Norton Co | Tunnel kiln |
US3183573A (en) * | 1960-07-26 | 1965-05-18 | Nat Tile & Mfg Co | Apparatus for making ceramic bodies and ceramic composition for use therewith |
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