US191005A - Improvement in furnaces - Google Patents
Improvement in furnaces Download PDFInfo
- Publication number
- US191005A US191005A US191005DA US191005A US 191005 A US191005 A US 191005A US 191005D A US191005D A US 191005DA US 191005 A US191005 A US 191005A
- Authority
- US
- United States
- Prior art keywords
- furnace
- chamber
- air
- wall
- section
- 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
- 239000000446 fuel Substances 0.000 description 18
- 238000002485 combustion reaction Methods 0.000 description 14
- 206010022000 Influenza Diseases 0.000 description 12
- 239000007789 gas Substances 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000010276 construction Methods 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 4
- 239000003830 anthracite Substances 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 206010022114 Injury Diseases 0.000 description 2
- 206010033799 Paralysis Diseases 0.000 description 2
- 239000002802 bituminous coal Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000002452 interceptive Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 238000005272 metallurgy Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003415 peat Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
Definitions
- the furnace is illustrated as applicable to purposes of metallurgy.
- A is the lower air-chamber; a, the inlet to same when compressed air is used; a, the fire-bars; a, a grating across the furnace, extending from the fire-bars to the under edge of the back wall; B, section of chamber from fire-bars to top of bridge-wall flues; b, section to under side of roof; b, the feed-way section; 0, the back wall; D, the front wall of section b,- E, a conduit, leading from section b,- e, inlet to conduit E; F, bridge-wall; G, bridge-wall flue; H, the upper air-chainber; h, outlet from same, placed at an angle in line of direction beyond the bridge-wall.
- FIG. 2 A, air-chamber, (lower;) a a a, fire-bars F, bridge-wall; G G, bridge-wall fines; D, front wall of section b; e e, inlets to conduit E; b, the feedway section, through the open end of which the feed is charged; I I, the side walls of furnace.
- FIG. 3 A, lower air-chamber; a, inlet when compressed air is used; a a a, fire-bars; a, a, grating under back wall G G, bridgewall flues; H, upper air-chamber; h, inlet to same; h h, outlets; II, side walls of furnace.
- the furnace is for the combustion of bituminous coal, peat, or other fuel in which hydrogen is a constituent element
- bituminous portion is convertible to the purposes of heat'in the gaseous state alone, while the carbonaceous portion, on the contrary, is combustible only in the solid state, and, what is essential to be borne in mind, neither can be consumed while they reare conducted to the bridge-wall flues G G. 7
- the charge of fuel settles, and in its descent, having parted with its volatile elements, the carbonaceous portion is acted upon by the air from chamber A entering through the firebars a. a a and the grating a a, the gaseous products being drawn, or, if compressed air is used,forced into and through the bridgewall flues.
- the gaseous products, drawn or forced from below, travel in direct line to the bridge-wall flues G G, while the furnace being kept closed at its top, and owing to the nature of its construction above that line, these currents from below cannot ascend higher, and. even should they contain free oxygen, the gases of distillation do not inflame.
- the air heated, or at the atmospheric temperature, is supplied to chamber H under pressure through a pipe in which is a slidevalve to regulate the quantity, and when the furnace is worked by compressed air, the supply for the combustion of the carbonaceous portion enters chamber A through opening a,
- the furnace performs at the same time the two important functions, neither interfering with the other-to wit, first, in the upper part the gaseous products of distillation, at high temperature, are produced by the direct action of the heated walls; and, second, in the lower part the gases of the carbonaceous portion are produced by the direct action of the air.
- this coal when charged in, fractures by the heat, and small particles are carried over the bridge-wall, wasting the fuel, and doing great injury to the metal in a working-chamber; or, if used for steam purposes, resulting in great waste, while each charge of fresh coal lowers the temperature to the extent that, for a period, the regular working of the furnace or the production of steam is paralyzed.
- the fuel of whatever variety, becomes gradually heated in its descent, and on reaching the lower part is in an incandescent state, and, therefore, in the proper condition for the rapid production of the gases of combustion.
- the management of the furnace The care to be observed is to properly regulate the admission of the air, to keep it charged full of fuel, and to have it settle regularly, the furnace being so accessible at the top through the charging-door, and "from below through the grating a. a, that perfect means are afforded to insure this; also through the grating a" a" the fire can be readily worked and kept clean and solid on the bars.
- the capacity of the furnace for the distilling process can be increased by giving additional height to section b, and by continuing the front wall D of section b down to the line of the top of the bridge-wall F, or lower, in which case the fire-bars a a a must be placed lower down, and the air-chamberAalso made deeper.
- These changes will be found desirable when the fuel to be used contains a high percentage of bituminous matter, since the capacity of section b being thereby increased, its contents are exposed for a longer time to the distilling action of the heated walls. They may also be made for the purpose of increasing the power of the furnace, or without reference to the characteristics of the fuel to be used.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion Of Fluid Fuel (AREA)
Description
V J. JENKINS;
FURNACE.
Patented May 22,1877.
To all whom it may concern eral custom.
UNIT D "STATES PATENT OFFICE JAMES JENKINS, OF BUFFALO, NEW YORK.
' IMPROVEMENT IN- FURNACES.
Specification forming partof Letters Patent N05. l9l.006, dated May 22, 1877; application filed October 16, 1876.
Be it known that-1', JAMES JENKINS, of thei city of Buflalo, in the county of Erie and State of New York, have invented an Improvement in Furnaces for the Combustion of Fuel, of i which the following isthespecifioation: p The drawings represent only the brick-work; of a furnace, working 'by'natural draft; but? when compressed air is used,the air-chamber is closed withradoor. In practice this brickwork is cased with iron' 'plates, as is the gen-' Figure 1 of the drawings is a longitudinal vertical section through the center; Fig. 2, a
vertical cross-section through the line AB; Fig. 3, a vertical cross-section thrbugh theline C D.
Like letters denote like parts wherever used.
The furnace is illustrated as applicable to purposes of metallurgy.
In Fig. 1, A is the lower air-chamber; a, the inlet to same when compressed air is used; a, the fire-bars; a, a grating across the furnace, extending from the fire-bars to the under edge of the back wall; B, section of chamber from fire-bars to top of bridge-wall flues; b, section to under side of roof; b, the feed-way section; 0, the back wall; D, the front wall of section b,- E, a conduit, leading from section b,- e, inlet to conduit E; F, bridge-wall; G, bridge-wall flue; H, the upper air-chainber; h, outlet from same, placed at an angle in line of direction beyond the bridge-wall.
In Fig. 2, A, air-chamber, (lower;) a a a, fire-bars F, bridge-wall; G G, bridge-wall fines; D, front wall of section b; e e, inlets to conduit E; b, the feedway section, through the open end of which the feed is charged; I I, the side walls of furnace.
In Fig. 3, A, lower air-chamber; a, inlet when compressed air is used; a a a, fire-bars; a, a, grating under back wall G G, bridgewall flues; H, upper air-chamber; h, inlet to same; h h, outlets; II, side walls of furnace.
The furnace, as illustrated, is for the combustion of bituminous coal, peat, or other fuel in which hydrogen is a constituent element,
7 and is also available for the use of anthracite hydrogen and carbon are united and solid.
Their respective characters and mode of entering into combustion are, however, essentially different. The first leading distinction is, that the bituminous portion is convertible to the purposes of heat'in the gaseous state alone, while the carbonaceous portion, on the contrary, is combustible only in the solid state, and, what is essential to be borne in mind, neither can be consumed while they reare conducted to the bridge-wall flues G G. 7
As the combustionon the fire-bars a a a pro- 'ceeds, the charge of fuel settles, and in its descent, having parted with its volatile elements, the carbonaceous portion is acted upon by the air from chamber A entering through the firebars a. a a and the grating a a, the gaseous products being drawn, or, if compressed air is used,forced into and through the bridgewall flues. The gaseous products, drawn or forced from below, travel in direct line to the bridge-wall flues G G, while the furnace being kept closed at its top, and owing to the nature of its construction above that line, these currents from below cannot ascend higher, and. even should they contain free oxygen, the gases of distillation do not inflame. Hence the products of distillation from above, in a gaseous state, conducted by conduits E E, and the products of combustion from below, partly inflamed and partly gaseous, meet and intermingle in the bridge-wall flues, to which they are drawn or forced, and are there met by jets of air under pressure from chamber H, through the outlets h h, producing perfect combustion and the maximum of heat.
The air heated, or at the atmospheric temperature, is supplied to chamber H under pressure through a pipe in which is a slidevalve to regulate the quantity, and when the furnace is worked by compressed air, the supply for the combustion of the carbonaceous portion enters chamber A through opening a,
being, in its arrangement and details, identical with what is in the usual practice.
Thus from the construction and operation of the furnace, it performs at the same time the two important functions, neither interfering with the other-to wit, first, in the upper part the gaseous products of distillation, at high temperature, are produced by the direct action of the heated walls; and, second, in the lower part the gases of the carbonaceous portion are produced by the direct action of the air.
The same construction is available for the use of anthracite fuel, although it contains no volatile element.
As at present used, this coal when charged in, fractures by the heat, and small particles are carried over the bridge-wall, wasting the fuel, and doing great injury to the metal in a working-chamber; or, if used for steam purposes, resulting in great waste, while each charge of fresh coal lowers the temperature to the extent that, for a period, the regular working of the furnace or the production of steam is paralyzed. With the furnace as described no such experience can be had, since being fed from the top, the fuel, of whatever variety, becomes gradually heated in its descent, and on reaching the lower part is in an incandescent state, and, therefore, in the proper condition for the rapid production of the gases of combustion.
The management of the furnace: The care to be observed is to properly regulate the admission of the air, to keep it charged full of fuel, and to have it settle regularly, the furnace being so accessible at the top through the charging-door, and "from below through the grating a. a, that perfect means are afforded to insure this; also through the grating a" a" the fire can be readily worked and kept clean and solid on the bars.
The capacity of the furnace for the distilling process can be increased by giving additional height to section b, and by continuing the front wall D of section b down to the line of the top of the bridge-wall F, or lower, in which case the fire-bars a a a must be placed lower down, and the air-chamberAalso made deeper. These changes will be found desirable when the fuel to be used contains a high percentage of bituminous matter, since the capacity of section b being thereby increased, its contents are exposed for a longer time to the distilling action of the heated walls. They may also be made for the purpose of increasing the power of the furnace, or without reference to the characteristics of the fuel to be used.
What I do claim as new, and desire to secure by Letters Patent, is-
The combination of the gas generating chamber 11 b, division D, provided with conduits e and passages E and G, with air-chamber H leading into said passage G, where the gases meet and intermingle with gases and flame from the main combustion-chamber, in the manner and for the purpose substantially as herein described.
JAMES JENKINS. Witnesses:
W. F. WHEELER, HENRY A. OBEVIST.
Publications (1)
Publication Number | Publication Date |
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US191005A true US191005A (en) | 1877-05-22 |
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Family Applications (1)
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US191005D Expired - Lifetime US191005A (en) | Improvement in furnaces |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060032817A1 (en) * | 1999-09-03 | 2006-02-16 | Tom Westberg | Separation apparatus |
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0
- US US191005D patent/US191005A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060032817A1 (en) * | 1999-09-03 | 2006-02-16 | Tom Westberg | Separation apparatus |
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