US282315A - James henbekson - Google Patents
James henbekson Download PDFInfo
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- US282315A US282315A US282315DA US282315A US 282315 A US282315 A US 282315A US 282315D A US282315D A US 282315DA US 282315 A US282315 A US 282315A
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- Prior art keywords
- air
- hearth
- fuel
- iron
- furnace
- Prior art date
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- 239000000446 fuel Substances 0.000 description 38
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 36
- 239000007789 gas Substances 0.000 description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 30
- 229910052742 iron Inorganic materials 0.000 description 18
- 239000000203 mixture Substances 0.000 description 18
- 229910001018 Cast iron Inorganic materials 0.000 description 16
- 238000002485 combustion reaction Methods 0.000 description 14
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- 229910000754 Wrought iron Inorganic materials 0.000 description 8
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 8
- 239000003830 anthracite Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 8
- CWYNVVGOOAEACU-UHFFFAOYSA-N fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 206010022000 Influenza Diseases 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 230000000875 corresponding Effects 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 230000036633 rest Effects 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 210000000614 Ribs Anatomy 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 4
- 235000015450 Tilia cordata Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000001535 kindling Effects 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- 230000001105 regulatory Effects 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 206010022114 Injury Diseases 0.000 description 2
- 210000001503 Joints Anatomy 0.000 description 2
- 241000758791 Juglandaceae Species 0.000 description 2
- 240000003936 Plumbago auriculata Species 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 229910052570 clay Inorganic materials 0.000 description 2
- 230000003247 decreasing Effects 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000011796 hollow space material Substances 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003472 neutralizing Effects 0.000 description 2
- 230000001590 oxidative Effects 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 230000000630 rising Effects 0.000 description 2
- 239000003566 sealing material Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 235000020234 walnut Nutrition 0.000 description 2
- 239000002699 waste material Substances 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
- F27B13/00—Furnaces with both stationary charge and progression of heating, e.g. of ring type, of type in which segmental kiln moves over stationary charge
- F27B13/02—Furnaces with both stationary charge and progression of heating, e.g. of ring type, of type in which segmental kiln moves over stationary charge of multiple-chamber type with permanent partitions; Combinations of furnaces
Definitions
- Fig. 9 is a plan of the same.
- FIG. 1 is a longitudinal section.
- Fig. 2 is ahorizontal section of the apparatus through the line a: w of Fig. .1.
- Fig. 3 is avertical transverse section on the line Y Y, on an enlarged scale, of Fig. 2.
- Fig. 4 is a plan view of the cast-iron truck, showing the ribs upon which the hearth V rests.
- Fig. 5 is a longi tudinal section of the gas and air passage in the outlet-neck of the producer.
- Fig. 6 is a plan view, and Fig. 7 a transverse vertical crosssection, of the same on an enlargedscale.
- Fig. Si a vertical cross-section of the hydraulic Fig. 10 is a plan view of the cast-iron plate supporting the roof of the reverberatory chamber 0.
- Fig. 11 is asectional view of the seal-joint which closes the space between the roof and hearth of the reverberatory chamber C.-
- the principal parts of the furnace repre sented in the said drawings are the gas-producer A, from which the flue B of the inletneck of the furnace is the outlet for the resulting gases, aswell as the inlet into the heatingchamber 0, the movable revolving hearth V, the flue D of the outlet-neck of the furnace to a second heating-chamber, E, the flue F of the outletneck of the second heating-chamber, G, beneath the boiler O, and thence through its flues to the chimney to the external air.
- the hearth or bottom of the furnace, V is moved vertically by being mounted on a table or platform, '12, raised and lowered by the upper end of a hydraulic ram, NV, and also has wheels on the bottom of the truck upon which it sets, so that it may be moved away from under the arch after being lowered.
- the top of the hydraulic rain is spherical, which fits into a corresponding socket in the bottom of the truck, and thus forms a pivot and a ball-and-socket joint, so that the hearth may revolve around it and be keptin its place when tipped to pour its contents.
- Thesurface of the wheels is beveled or inclined to correspond to the bevel or inclination of the track.
- the brackets are arranged, as shown,
- Wooden disks may be placed between the wheels and the outside bracket to take up the friction.
- the hearth is revolved by means of the spurwheel a, working in corresponding teeth in the rim of the hearth.
- the hearth is main- A plattained in its vertical position by the guideplate m and the four guide-rods 0', passing through it.
- the hearth when in its raised position in the furnace, is sealed, so that there i cannot be-any passage of heat or gases from it to the external air, by an annular open box, a, at the top, filled with sand or water, in which a ring, 6', on the bottoin plate, Z.
- Fig. 3 supporting the chamber 0, dips nearly to the bottom.
- the plate is provided near its inner edge with an iron pipe or passage, Z, cast therein, inwhich water or air circulates to cool the plate and heat of the furnace.
- Fig. 10 is a plan View of the plate Z, showing the cooling-chamber in dotted lines, and
- Fig. 11 is a sectional view of the sealed joint made by the ring 1; on the bottom, dipping into the annular box a.
- the hearth V is preferably divided in two parts.
- the hearth proper, in which the iron is treated, is preferably made of rolled plate of pure soft steel low in carbon and having great extension under pulling stress, (say under 0.10
- This pan or hearth rests in the cast-iron platform upon raised ribs or projections 1), (shown in Fig. 4,) and the platform, having the sides reaching to the under side of the lower spout or tap-hole of the hearth, forms a shallow dish, which enables the use of water or air therein for cooling the bottom of the hearth. If desired, there is a narrow open space about one inch wide, surrounding the hearth, and between it and the sides of the'pan, which enables the ingress or egress of air for cooling the hearth, if air is used.
- the air or water is introduced through the opening in middle of the hydraulic ram, as hereinafter described.
- the movable hearth or bottom V is provided with a lining, a, of refractory material, which may be coke or plumbago and fire-clay, (such as is used for steel-melting crucibles,) oxide of iron, lime, magnesian lime, magnesia, sand, or silicious linings, depending upon theamount of heat required and the kind of When reagents are used they are generally spread over this lining by introducing them through the door d, or by lowering the hearth from the chamber C for that purpose.
- the iron used or treated may be placed in the hearth in the same way, or the roof may be made movable and removed for these purposes.
- the gases employed to heat the reverberatory chamber 0 and convert the charge enter through the flue B.
- the combustible gases pass from fine B, descending thence, by the vertical fines f f, to chamber 0.
- these gases are mixed with regulated quantities of atmospheric air, preferably heated to from 700 to 1200 Fahrenheit, whereby the gases are inflamed and perfect combustion produced.
- the heated air passes into such flues or passages ff from the tuyeres h, Figs. 5, 6, and 7, which communicate at their rear with airpassages to a flue, m, and thence by the pipe T,
- the gas-producer A is constructed at one end of the'reverberatory furnace.
- Theinterior of the gasproducer is formed of two fuelchambers, 1'1", the former, r, being beneath the iron reservoir or hopper 1", and being therefore designated the lower fuelchamber, while the hopper or reservoir r is a distinct fuel-chamber, where a different gas process is carried on. It is therefore designated as the upper fuel-chamber.
- the interior of the gasproducer A shall at all times when working be charged to the top with fuel, that will fall automatically as it burns away at the bottom, thus supplying the'fire, while the fuel becomes gradually heated, decreasing in temperature to the top.
- a is the top of the fuel-hopper; b, a weighted lever to close the hopper air-tight by raising the cone 0 when charging the fuel at a.
- d is a port or opening at the bottom of the gas-producer, for removing the contents and igniting the fuel.
- a pun1p, t is attached to the crank-shaft of the blast-engine s, which pumps at each revolution a certain regulated required amount of Water.
- the revolution of the blastengine 8 pumps a certain amount of air, and also pumps a certain required amount of water.
- the water passes through a pipe, Q, placed in the front end of the boiler-fine, to the rear end, and thence under the boiler back to the front in zigzag vertical form, and near the end terminates in a coil, Q.
- This arrangement enables all of the water to be gradually converted into steam and to become highlysuperheated steam by the time it reaches the end of the coil.
- the superheated steam then passes through a covered pipe (not shown in the drawings) to the tuyere h in a highly-sup erheated state, or at a temperature of 600 to 800 Fahrenheit, and thence into the gas-producer among the incandescent fuel, where it decomposes to hydrogen and oxygen, the latter combining with part of the carbon of the fuel to form carbonicoxide.
- the carbonic oxide and hydrogen thus produced mix with the carbonic oxide formed by the combustion ofthe fuel with the air from thertuyeres, and pass from the producer through the flue B to the fines f, where they areburned with heated air.
- the part where steam is 'formed should beof wroughtiron, as the superheated steam rapidly oxidizes wrought-iron and has but little effect on cast-iron, and as there is practically no appreciable pressure used, cast-iron is better than wrought-iron for this purpose.
- I preferably effect the combustion'of the gases passing through the outletB by air supplied by a distinct blast-machine, of which I is the steam-cylinder, and J the air-cylinder, thepistons being connected by a cross-head.
- the air passes from the blast-cylinder through an airronduit system, as follows: K is an airreceiver, into which the air is delivered from the blast-machine J in a measured quantity.
- the pipe L delivers the air, when perfect combustion with a neutral or oxidizing flame is required, to vertical cast-iron pipes S, Fig. 1, ranged under the boiler along the side walls, as shown in the plan in Fig. 2.
- the blast enters the rear end and passes up and down through these pipes, which are heated by the waste or spent gases of the furnace. thus heated passes from the pipes to the pipe T, thence to the channel at, Fig. 5, inthe out- Figs. 5, 6, and 7, where it impingesupon the gases passing throughthe flue B and the vertical fiues f f
- the blast-machine should deliver to the cast-iron air-heating apparatus about four hundred and forty-five cubic feet of air to burn each pound of hydrogen in the anthracite and that produced by the decomposition of the su perheated steam, and 7 2.5 cubic feet of air for each pound of carbon converted into carbonic oxide in the producer by the oxygen of the air and of the decomposed superheated steam therein acting upon the incandescent fuel; and when an oxidizing-flame with less heat is required a greater quantity of air should be used. If one-half more air is used, the temperature is reduced'to about two-thirds of that realized from the use of the above proportions.
- Fig. 8 shows the hydraulic ram of Fig. l on an enlarged scale for raising and loweringthe The air hearth V of the furnace.
- the head of the ram metal or iron is used, care being taken to make either air or water tight joints.
- the ram is recessed slightly below the head to allow it to turn in the socket and keep the j oint tight.
- f is a central passage in the ram, through which the air or water passes in or out of the table or platform 4).
- the airor wa ter is pumped through the passage f of the ram to the space beneath the wrought-iron hearth V and cools it. as far as the table ex tends up its sides.
- the platform rests upon thetop of the ram, which fits in its socket and on the shoulder z.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Solid-Fuel Combustion (AREA)
Description
(No Model) '3 Sheets-Sheet 1.' J. HENDERSON.
FURNACE THE MANUFACTURE OF IRON AND. STEEL AND FOR.
. OTHER PURPOSES. No. 282,315. N PatentedJ u1y'31.1883,
N. PETERS Phu'o-Lilhugnpl c.
mo Model.) -J. HENDERSON.
FURNACE FOR THE MANUFACTURE OF IRON AND STEEL AND FOR 3 SheetsSheet 2.
OTHER PURPOSES.
No. 282,315. Patented J-uly 81.1883.
WITNESSES N. PETERS. FIIMo-Uthogmpiur. wa-hin nm, DJ;
UNITE STATES JAMES nnnnnn'son, or BELLEFONTE, PENNSYLVANIA.
PATENT Orricn. V
FURNACE FOR THE MANUFACTURE OF IRQN AND STEEL AND FOR OTHER PURPOSES.
SPECIFICATION forming part of Letters Patent No. 282,315, dated July 31, 1883.
- Application filed June 29,1se3. (No model.)
To all whom it may concern.-
Be it known that I, JAMES HENDERSON, of Bellefonte, county of Centre, and State of Pennsylvania, have invented certain new and useful Improvements in Furnaces for the Manufacture of Iron and Steel, and for other purram, and Fig. 9 is a plan of the same.
poses, of which the following issuch specification as will enable those skilled in the art to understand and practice the same, being a division of application N 0. 87,393, filed March 2, 1883. l
This my invention consists of novel combinations of elements in apparatuses for metal lurgical andother uses, as shown in drawings, in which- Figure 1 is a longitudinal section. Fig. 2 is ahorizontal section of the apparatus through the line a: w of Fig. .1. Fig. 3 is avertical transverse section on the line Y Y, on an enlarged scale, of Fig. 2. Fig. 4: is a plan view of the cast-iron truck, showing the ribs upon which the hearth V rests. Fig. 5 is a longi tudinal section of the gas and air passage in the outlet-neck of the producer. Fig. 6 is a plan view, and Fig. 7 a transverse vertical crosssection, of the same on an enlargedscale. Fig. Sis a vertical cross-section of the hydraulic Fig. 10 is a plan view of the cast-iron plate supporting the roof of the reverberatory chamber 0. Fig. 11 is asectional view of the seal-joint which closes the space between the roof and hearth of the reverberatory chamber C.-
The same letters refer to the same parts in the different figures.
The principal parts of the furnace repre sented in the said drawings are the gas-producer A, from which the flue B of the inletneck of the furnace is the outlet for the resulting gases, aswell as the inlet into the heatingchamber 0, the movable revolving hearth V, the flue D of the outlet-neck of the furnace to a second heating-chamber, E, the flue F of the outletneck of the second heating-chamber, G, beneath the boiler O, and thence through its flues to the chimney to the external air.
The hearth or bottom of the furnace, V, is moved vertically by being mounted on a table or platform, '12, raised and lowered by the upper end of a hydraulic ram, NV, and also has wheels on the bottom of the truck upon which it sets, so that it may be moved away from under the arch after being lowered.
The top of the hydraulic rain is spherical, which fits into a corresponding socket in the bottom of the truck, and thus forms a pivot and a ball-and-socket joint, so that the hearth may revolve around it and be keptin its place when tipped to pour its contents. form, a, with wheels upon the top, fitted in brackets, carries the hearth when it revolves by means of a track corresponding to the :wheels, cast on the under side of the hearth.
Thesurface of the wheels is beveled or inclined to correspond to the bevel or inclination of the track. The brackets are arranged, as shown,
with hollow space for water, in which the wheel revolves. Wooden disks may be placed between the wheels and the outside bracket to take up the friction.
The hearth is revolved by means of the spurwheel a, working in corresponding teeth in the rim of the hearth. The hearth is main- A plattained in its vertical position by the guideplate m and the four guide-rods 0', passing through it. The hearth, when in its raised position in the furnace, is sealed, so that there i cannot be-any passage of heat or gases from it to the external air, by an annular open box, a, at the top, filled with sand or water, in which a ring, 6', on the bottoin plate, Z. Fig. 3, supporting the chamber 0, dips nearly to the bottom. The plate is provided near its inner edge with an iron pipe or passage, Z, cast therein, inwhich water or air circulates to cool the plate and heat of the furnace.
Fig. 10 is a plan View of the plate Z, showing the cooling-chamber in dotted lines, and
Fig. 11 is a sectional view of the sealed joint made by the ring 1; on the bottom, dipping into the annular box a.
The hearth V is preferably divided in two parts. The hearth proper, in which the iron is treated, is preferably made of rolled plate of pure soft steel low in carbon and having great extension under pulling stress, (say under 0.10
per cent. of carbon, with twenty-five percent. extension under strain,) to enable it to expand and contract with heating and cooling without prevent injury from the operation performed therein.
liability of bursting. This pan or hearth rests in the cast-iron platform upon raised ribs or projections 1), (shown in Fig. 4,) and the platform, having the sides reaching to the under side of the lower spout or tap-hole of the hearth, forms a shallow dish, which enables the use of water or air therein for cooling the bottom of the hearth. If desired, there is a narrow open space about one inch wide, surrounding the hearth, and between it and the sides of the'pan, which enables the ingress or egress of air for cooling the hearth, if air is used.
The air or water is introduced through the opening in middle of the hydraulic ram, as hereinafter described.
The movable hearth or bottom V is provided with a lining, a, of refractory material, which may be coke or plumbago and fire-clay, (such as is used for steel-melting crucibles,) oxide of iron, lime, magnesian lime, magnesia, sand, or silicious linings, depending upon theamount of heat required and the kind of When reagents are used they are generally spread over this lining by introducing them through the door d, or by lowering the hearth from the chamber C for that purpose. The iron used or treated may be placed in the hearth in the same way, or the roof may be made movable and removed for these purposes.
The gases employed to heat the reverberatory chamber 0 and convert the charge enter through the flue B. The combustible gases pass from fine B, descending thence, by the vertical fines f f, to chamber 0. In the flues ff these gases are mixed with regulated quantities of atmospheric air, preferably heated to from 700 to 1200 Fahrenheit, whereby the gases are inflamed and perfect combustion produced. From the chamber 0 the products of combustion are conveyed away by the flue D. The heated air passes into such flues or passages ff from the tuyeres h, Figs. 5, 6, and 7, which communicate at their rear with airpassages to a flue, m, and thence by the pipe T,
Figs. 1 and 2, to the cast-iron air-heating pipes S, placed at each side of the boiler-chamber G, where the air is heated by the spent gases from the furnace, (or the air may be heated in any other suitable air-heating apparatus, either attached to or detached from the furnace,) which is connected with a pipe, L, leading from the blast-receiver K.
The gas-producer A is constructed at one end of the'reverberatory furnace. Theinterior of the gasproducer is formed of two fuelchambers, 1'1", the former, r, being beneath the iron reservoir or hopper 1", and being therefore designated the lower fuelchamber, while the hopper or reservoir r is a distinct fuel-chamber, where a different gas process is carried on. It is therefore designated as the upper fuel-chamber. It isdesigned that the interior of the gasproducer A shall at all times when working be charged to the top with fuel, that will fall automatically as it burns away at the bottom, thus supplying the'fire, while the fuel becomes gradually heated, decreasing in temperature to the top. a is the top of the fuel-hopper; b, a weighted lever to close the hopper air-tight by raising the cone 0 when charging the fuel at a. d is a port or opening at the bottom of the gas-producer, for removing the contents and igniting the fuel.
In operating the apparatus kindling is inserted at d and the fuel at a. The kindling being ignited, the fuel-blower N is brought into action. The air from it passes bya pipe to a reservoir, P, to equalize the pressure, and thence by a pipe surrounding the gas-producer. From this circular pipe the air enters the lower fuel-chamber, a", through the air-passages or tuyeres i i, and acts upon the fuel in the gasproducer, decomposing the fuel. The gases resulting from the decomposition, rising up through the interstices of the fuel, escape by the gas-flue B and gas-channels f f into the reverberatory chamber. The heat incident to the decomposition of fuel in the lower fuelchamber, 1, acts upon the fuel in the coal-reservoir or upper fuel-chamber, r, effecting a distillation of the fuel therein and causing the fuel to evolve gases. These gases are forced, by the pressure made by their distillation, down and into contact with the incandescent fuel in the chamber 7', whereby the tarry matterstherein become decomposed and pass with the other gases through the annular space between the retort and the wall of the gas-producer, and pass thence into the space about the upper retort to the flue B. As perfect combustion of carbonic oxide is effected when mixed with one-third of its volume of hydro gen, I use, preferably, superheated steam in regular measured proportions, injected through one or more tuyeres, h, in the gas-producer, from twelve to twenty inches above the air-tuyeres i i, when cold air is used and the fuel is of small size, (if coke or anthracite, of
size of walnuts.) A pun1p, t, is attached to the crank-shaft of the blast-engine s, which pumps at each revolution a certain regulated required amount of Water. The revolution of the blastengine 8 pumps a certain amount of air, and also pumps a certain required amount of water. The water passes through a pipe, Q, placed in the front end of the boiler-fine, to the rear end, and thence under the boiler back to the front in zigzag vertical form, and near the end terminates in a coil, Q. This arrangement enables all of the water to be gradually converted into steam and to become highlysuperheated steam by the time it reaches the end of the coil. The superheated steam then passes through a covered pipe (not shown in the drawings) to the tuyere h in a highly-sup erheated state, or at a temperature of 600 to 800 Fahrenheit, and thence into the gas-producer among the incandescent fuel, where it decomposes to hydrogen and oxygen, the latter combining with part of the carbon of the fuel to form carbonicoxide. The carbonic oxide and hydrogen thus produced mix with the carbonic oxide formed by the combustion ofthe fuel with the air from thertuyeres, and pass from the producer through the flue B to the fines f, where they areburned with heated air. About three-fourths of a cubicinch of water reduced to sup erheatedsteam is the proportion that I have found-with four feet of cubicair introduced in the lower part of the gas-producer 1*, with anthracite to give the required proportions of hydrogen and carbonicoxide-to produce perfeet combustion when burned with sufficient 21111.
In: order to increase the durability of the superheating apparatus, the part where the sup erheating takes place, and from thence leading tothegas producer,should bemadeofcastiron. The part where steam is 'formed should beof wroughtiron, as the superheated steam rapidly oxidizes wrought-iron and has but little effect on cast-iron, and as there is practically no appreciable pressure used, cast-iron is better than wrought-iron for this purpose.
let-neck of the gas-producer, tothe tuyeres h,
I preferably effect the combustion'of the gases passing through the outletB by air supplied by a distinct blast-machine, of which I is the steam-cylinder, and J the air-cylinder, thepistons being connected by a cross-head. The air passes from the blast-cylinder through an airronduit system, as follows: K is an airreceiver, into which the air is delivered from the blast-machine J in a measured quantity. The pipe L delivers the air, when perfect combustion with a neutral or oxidizing flame is required, to vertical cast-iron pipes S, Fig. 1, ranged under the boiler along the side walls, as shown in the plan in Fig. 2. The blast enters the rear end and passes up and down through these pipes, which are heated by the waste or spent gases of the furnace. thus heated passes from the pipes to the pipe T, thence to the channel at, Fig. 5, inthe out- Figs. 5, 6, and 7, where it impingesupon the gases passing throughthe flue B and the vertical fiues f f.
When the fuel used in the gas-producer is anthracite and the greatest intensity of heat is required, the blast-machine should deliver to the cast-iron air-heating apparatus about four hundred and forty-five cubic feet of air to burn each pound of hydrogen in the anthracite and that produced by the decomposition of the su perheated steam, and 7 2.5 cubic feet of air for each pound of carbon converted into carbonic oxide in the producer by the oxygen of the air and of the decomposed superheated steam therein acting upon the incandescent fuel; and when an oxidizing-flame with less heat is required a greater quantity of air should be used. If one-half more air is used, the temperature is reduced'to about two-thirds of that realized from the use of the above proportions.
Fig. 8 shows the hydraulic ram of Fig. l on an enlarged scale for raising and loweringthe The air hearth V of the furnace. The head of the ram metal or iron is used, care being taken to make either air or water tight joints. The ram is recessed slightly below the head to allow it to turn in the socket and keep the j oint tight. f is a central passage in the ram, through which the air or water passes in or out of the table or platform 4). The airor wa ter is pumped through the passage f of the ram to the space beneath the wrought-iron hearth V and cools it. as far as the table ex tends up its sides. The platform rests upon thetop of the ram, which fits in its socket and on the shoulder z. When it is desired to pour the contents of the pan or hearth, if water is used, the water is run out of the table through openings f, l and theram lowered by discharg- 0'is spherical and fits into a socket in the ing the water from the chambers g and g, the
ters Patent, is-
l. The combination of a movable hearth, guide-plate an, their intermediate connecting meeh anism, and the gui derods 0, substantially as specified.
2. The combination of a hydraulic ram with ball top and hollow center and atable and hollow socket communicating with a coolingehamber beneath the hearth of the furnace, substantially as described.
3. The combination, in a gas-furnace, of. the boiler, the hot-blast pipe, and the superheater both beneath said boiler, as specified.
4. The hearth provided with means for rotating the same, and the rollers and recessed brackets, in combination with the platform a",
' substantially as described.
5. The hydraulic ram with ball top, in combination with table and socket and hearth, substantially as described.
6. The hydraulic ram with ball top, in eombination with a socket-joint, with the platform a and table and hearth, substantially as specifled. a
.7. In combination with the hearth of a metallurgieal furnace and a supporting-table, the hydraulic ram with ball top and hollow center, as described. q
8. In combination with the hearth of amet- What I claim, and desire to secure by Let allurgieal furnace and a supporting-table, the duplex hydraulic ram with ball top and hollow center and two water-chambers, substantially as described. y a
9. The seal-joint formed by the ring-plate on which the walls of the reverberatory chamber rest, in which is a cooling-chamber, and annular groove containing a sealing material, the upper edge of the hearth provided With am into which a circular downwardly-projecting 1o annular groove containing a sealingmaterml, 11p on the ring-plate d1ps,- substantially as substantially as specified. specified. I
5 10. The seal-joint formed by the ring-plate J AMES HENDERSON.
011 which the walls of the reverberatory cham- Witnesses: her rest, in which is a cooling-chmnber, and JOSEPH J. SULLIVAN,
the upper edge of the hearth provided with an JOHN 'E. ELMENDORF.
Publications (1)
Publication Number | Publication Date |
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US282315A true US282315A (en) | 1883-07-31 |
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US282315D Expired - Lifetime US282315A (en) | James henbekson |
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US (1) | US282315A (en) |
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