US320908A - Fotjeth to d estaing s - Google Patents
Fotjeth to d estaing s Download PDFInfo
- Publication number
- US320908A US320908A US320908DA US320908A US 320908 A US320908 A US 320908A US 320908D A US320908D A US 320908DA US 320908 A US320908 A US 320908A
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- Prior art keywords
- sump
- lead
- chamber
- conveyer
- ores
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- Expired - Lifetime
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- 238000002485 combustion reaction Methods 0.000 description 14
- 238000003723 Smelting Methods 0.000 description 12
- 239000007788 liquid Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 239000010970 precious metal Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000000428 dust Substances 0.000 description 8
- 230000004907 flux Effects 0.000 description 8
- 239000002893 slag Substances 0.000 description 8
- 239000012141 concentrate Substances 0.000 description 6
- 239000003517 fume Substances 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000007921 spray Substances 0.000 description 6
- 229920002456 HOTAIR Polymers 0.000 description 4
- 239000011449 brick Substances 0.000 description 4
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 4
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 2
- 210000002370 ICC Anatomy 0.000 description 2
- 210000003800 Pharynx Anatomy 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000002459 sustained Effects 0.000 description 2
- 150000004772 tellurides Chemical class 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/001—Dry processes
- C22B7/004—Dry processes separating two or more metals by melting out (liquation), i.e. heating above the temperature of the lower melting metal component(s); by fractional crystallisation (controlled freezing)
Definitions
- My invention relates to smelting ores, and has for its object to improve and simplify the manner and means for smelting, so that all manner of ores carrying lead, gold, or silver, or a combination of any and all of them, may be economically treated; and to this end my invention consists in the methods and means hereinafter pointed out for producing these effects.
- Figure 1 is a plan view of the furnace, partlyin section, and Fig. 2 is a longitudinal section on the lines at m, Fig. 1.
- a sump or crucible, A is formed in the shape of a basin or dish, and is made of common red or fire brick, and is surrounded by the proper amount of masonry of the usual red-brick work.
- the interior of the sump may be lined with any usual or suitable material that will not contract or expand under the heat or allow the molten metal to penetrate or escape from it.
- a lead-well At the side of the sump, and connected to its bottom by a suitable passage, is arranged a lead-well, thetop of which is of such a height as to allow the excess of lead to overflow and maintain the molte11 lead in the sump at a proper level.
- This level is preferably about two inches from the top of the sump, and this space is occupied by a molten matte or blanket of fluxes and reagents, serving as a covering to protect the bat-h of lead from scorification; also as a bed upon which to effect the final separation of the metallic constituents of ores from the gangue, matrix, or core contained therein.
- the sump is covered with an arch having suitable openings to connect with the fire-boxes and expansion-chamber.
- a slag tap-hole, B, and a matte tap-hole, C are formed at the base of the arch, and a peep-hole, O, is 10- rated in a suitable position to allow the workman to watch the operations.
- fireboxes consist of proper masonrywork, forming the ash-pit T, the fire-place I having the grate-bars R supported in the walls, an arched covering, Q, made to rest upon the walls, and provided with a suitable door, U,
- a slash bar-hole, V for stirring the fire, an opening for the superheated steam and oil pipes ⁇ V, and in the top of the arch an opening supplied with.
- any of the ordinary feeding devices for feeding the fuel directly into the middle of fire-place.
- the top of the arch is contracted at the end, as seen at a, where it enters the sumparch, for the purpose of concentrating in a blow-pipe manner the heat and flames, as more particularly set forth hereinafter.
- Suitable doors for regulating the draft and disposing of the ashes may be arranged in any desired manner.
- the oreconveyer, desulphurizer, expansion and con- (lensing chambers, and other appliances for completing the smelting process are arranged on the opposite side of the sump.
- the ore-conveyer F consists of a long tube or cylinder perforated at intervals throughout its length, as at H H, provided with a suitable hopper, I, and ascrew-shaft, G, adapted to be rotated by suitable means, as pulley G.
- the inner end of the tube or pipe extends within the sump-arch and over the matte and lead-well.
- an expansion or dust chamber, K through which the products of combustion are drawn, and from which they pass into the condensingchamber L through the inlet-holes D, where they are subjected to a spray or stream of water, whence the fumes and heat pass through the outlet-hole M, being drawn therethrough by suitable exhausting apparatus, as a fan.
- Any precious metal that has been carried by the fumes into the condensing-chamber will be deposited by the spray or stream of water into the condensing-chamber, and, passing through the hole N, will be carried into the settling-pans, where it is gathered ina manner well understood, and is preferably placed in a bag, when it is passed directly into the center of the combustion chamber by being dropped through the hole P in the top of the sump-arch.
- the lead-well being filled and the mattebeing supported upon the lead, and the fires in the fire-boxes being kindled,the ore, and fluxes, when necessary, is fed into the hopper I of the conveyer pipe or tube, and the screw-conveyer being turned by proper means, the ore is slowly fed toward the interior of the sump.
- the desulphurizing process is completed, and it passes out of the conveyer in a liquid or semiliquid form, when it meets the flames and heat from the fire-boxes, the boxes being arranged and constructed, as before set forth, so as to direct the flames at this point, and the smelting takes place in the combustion-chamber of the sump-arch, the molten matte or blanket acting as a separating agent.
- the ore in its molten or semi-molten state falls upon this blanket, and in passing over it to the slag taphole precipitates its metals into the blanket, the precious metals, owing to their greater specific gravity, going through into the lead-well and to the dipping-cup, while the refuse or slag, being lighter than the matte, passes over the top of it out of the slag-holes.
- the vaporizable products of combustion are drawn by the exhaust apparatus through the smoke-space,heating the ore-conveyer and desulphurizing the ore; thence they pass to the dust or expansion chamber, thence through the openings D into the condensingchamber L, where they come in contact with a spray or stream of water and pass through the outlet-hole M into the chimney.
- the precious metals contained therein, being deposited into the bottom of the condensingchamber pass through the water discharge hole N into suitable separating-pans or settling-tanks, as before stated.
- the volume of the bath increases by the reduction of lead in the stock treated, it is dipped from the lead-well E or allowed to overflow into molds, and is ready to ship as base bullion; or it may be run over a series of refining-plates and the precious metals separated from the base or lead bullion.
- a very important feature of my invention is the molten matte or blanket contained in the sump above'the lead.
- Thisblanket or matte is formed automatically from the various reagents .fed with or found in the ores, and when once formed is permanent, its volume being sustained from the ores fed to the furnace, and any excess or surplus flowing off by the matte tap-hole, which is continuously open.
- the lead in the sump is automatically maintained at the proper level, and the blanket or matte is also automatically maintained, and thereby the lead is always properly covered by the matte, preventing scorification, and the slag freely flows off at the open slag-hole.
- the heat and flames from the fuel used are carried from the fire-boxes through the funnel -shaped throats into the combustion chamber, where they meet, being concentrated upon the smeltingpoint, and crossing each other in the sump they produce a sort of rotary flame, which is practically confined within the sump-arch above the blanket, and I am thereby enabled to utilize the greatest amount of heat and at the most effectual point.
- Another feature of my invention consists in using an exhaust or suction blower instead of a blast-blower, and by this means, while Iain enabled to keep up the requisite amount of draft for the furnaces, the blanket or matte is not seriously disturbed or broken, as when the blast is used, and scorifieation and loss of the lead is prevented. Moreover, on account of the arrangement of the furnaces and sumparch as above indicated, I am enabled to draw the waste products of combustion and theheat through the expansion-chamber around the ore-conveyer more in the form of heated gases, as very little, if any, flame escapes from the sump-arch. This I find is very advantageous in reducing or desulphurizing them in the conveyer.
- ⁇ Vhere fluxes are necessary I mix them with the ores in the conveyer, and thereby avoid the necessity of feeding them separately to the reducing-point.
- the hole P in the top of the sump-arch enables me to feed rich stock-such as the tellurides, chlorides, Ste-without loss directly into the lead bath.
- I am aware ore has been fed through a cylinder, where it was roasted in contact with hot air to charge it with oxygen, and then fed into another cylinder and roasted in direct contact with a flame, the sulphur being largely consumed and fluxes being added therein, and
- the combination with a sump and .fireboxes connected therewith, arranged to concentrate the flames and heat in the sump, of a smoke or dust chamber containing an oreconveyer, a condensing chamber connected therewith, an exhausting apparatus connected with the condensing-chamber, whereby the flames and heat are drawn into the sump and concentrated, and the products of combustion are drawn through the chambers, and means for supplying water to the condensingcham ber, as and for the purpose set forth.
- the combination,with the sump contain ing a lead bath and a metallic blanket, of fire-boxes connected to said sump and a sumparch having an opening at the top and an oreconveyer located in the smoke-chamber,whereby the ordinary ores may be conveyed to the sump in a semi-liquid state, and the rich ores may be dropped directly into the sump at the smelting-point, substantially as described.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
(No Model.) 2 Sheets-Sheet 1.
M. D. BRETT.
SMELTING oRl-"Js.
No. 320,908. atnted June 30, 1885 oumo n hnr. wahingwm n1;
(No Model.) 2 Sheets-Sheet 2. M. D. BRETT.
SMELTING ORES. No. 320,908. Patented June 30, 188 5.
UNITED STATES PATENT OFFICE.
MATHEW DAUSON BRETT, OF DENVER, COLORADO, ASSIGNOR OF ONE- FOURTH TO DESTAING S. COVERT, OF SAME PLACE.
SMELTI'NG ORES.
SPECIFICATION forming part; of Letters Patent No. 320,908, dated June 30, 1885,
(No model.)
To all whmn it may concern:
Be it known that I, MATHEW D. BRETT, a citizen of the United States, residing at Denver, Arapahoe county, State of Colorado, have invented certain new and useful Improvements in Smelting Ores,of which the following is a specification.
My invention relates to smelting ores, and has for its object to improve and simplify the manner and means for smelting, so that all manner of ores carrying lead, gold, or silver, or a combination of any and all of them, may be economically treated; and to this end my invention consists in the methods and means hereinafter pointed out for producing these effects.
I11 the accompanying drawings, forming part of this specification, Figure 1 is a plan view of the furnace, partlyin section, and Fig. 2 is a longitudinal section on the lines at m, Fig. 1.
A sump or crucible, A, is formed in the shape of a basin or dish, and is made of common red or fire brick, and is surrounded by the proper amount of masonry of the usual red-brick work. The interior of the sump may be lined with any usual or suitable material that will not contract or expand under the heat or allow the molten metal to penetrate or escape from it. At the side of the sump, and connected to its bottom by a suitable passage, is arranged a lead-well, thetop of which is of such a height as to allow the excess of lead to overflow and maintain the molte11 lead in the sump at a proper level. This level is preferably about two inches from the top of the sump, and this space is occupied by a molten matte or blanket of fluxes and reagents, serving as a covering to protect the bat-h of lead from scorification; also as a bed upon which to effect the final separation of the metallic constituents of ores from the gangue, matrix, or core contained therein. The sump is covered with an arch having suitable openings to connect with the fire-boxes and expansion-chamber. A slag tap-hole, B, and a matte tap-hole, C, are formed at the base of the arch, and a peep-hole, O, is 10- rated in a suitable position to allow the workman to watch the operations. Outside of the walls of the sump are located several fireboxes, Q, two being shown in the drawings. These fire-boxes consist of proper masonrywork, forming the ash-pit T, the fire-place I having the grate-bars R supported in the walls, an arched covering, Q, made to rest upon the walls, and provided with a suitable door, U,
preferably having a slash bar-hole, V, for stirring the fire, an opening for the superheated steam and oil pipes \V, and in the top of the arch an opening supplied with. any of the ordinary feeding devices for feeding the fuel directly into the middle of fire-place. The top of the arch is contracted at the end, as seen at a, where it enters the sumparch, for the purpose of concentrating in a blow-pipe manner the heat and flames, as more particularly set forth hereinafter. Suitable doors for regulating the draft and disposing of the ashes may be arranged in any desired manner. On the opposite side of the sump are arranged the oreconveyer, desulphurizer, expansion and con- (lensing chambers, and other appliances for completing the smelting process.
The ore-conveyer F consists of a long tube or cylinder perforated at intervals throughout its length, as at H H, provided with a suitable hopper, I, and ascrew-shaft, G, adapted to be rotated by suitable means, as pulley G. The inner end of the tube or pipe extends within the sump-arch and over the matte and lead-well. Around the conveyer is formed an expansion or dust chamber, K, through which the products of combustion are drawn, and from which they pass into the condensingchamber L through the inlet-holes D, where they are subjected to a spray or stream of water, whence the fumes and heat pass through the outlet-hole M, being drawn therethrough by suitable exhausting apparatus, as a fan. Any precious metal that has been carried by the fumes into the condensing-chamber will be deposited by the spray or stream of water into the condensing-chamber, and, passing through the hole N, will be carried into the settling-pans, where it is gathered ina manner well understood, and is preferably placed in a bag, when it is passed directly into the center of the combustion chamber by being dropped through the hole P in the top of the sump-arch.
The operation of my furnace is as follows:
The lead-well being filled and the mattebeing supported upon the lead, and the fires in the fire-boxes being kindled,the ore, and fluxes, when necessary, is fed into the hopper I of the conveyer pipe or tube, and the screw-conveyer being turned by proper means, the ore is slowly fed toward the interior of the sump. The products of combustion at the same time, passing through the smoke-chamber around the conveyer, heat the same and desulphurize the ore in the conveyer, the fumes escaplng by the fume-holes H H, and pass through the dust and condensing chambers K L, being drawn therethrough by the exhausting apparatus. As the ore is slowly fed through the conveyer, the desulphurizing process is completed, and it passes out of the conveyer in a liquid or semiliquid form, when it meets the flames and heat from the fire-boxes, the boxes being arranged and constructed, as before set forth, so as to direct the flames at this point, and the smelting takes place in the combustion-chamber of the sump-arch, the molten matte or blanket acting as a separating agent. The ore in its molten or semi-molten state falls upon this blanket, and in passing over it to the slag taphole precipitates its metals into the blanket, the precious metals, owing to their greater specific gravity, going through into the lead-well and to the dipping-cup, while the refuse or slag, being lighter than the matte, passes over the top of it out of the slag-holes. The vaporizable products of combustion are drawn by the exhaust apparatus through the smoke-space,heating the ore-conveyer and desulphurizing the ore; thence they pass to the dust or expansion chamber, thence through the openings D into the condensingchamber L, where they come in contact with a spray or stream of water and pass through the outlet-hole M into the chimney. The precious metals contained therein, being deposited into the bottom of the condensingchamber, pass through the water discharge hole N into suitable separating-pans or settling-tanks, as before stated.
From the above the advantages of my improved furnace are apparent. I use but one hearth or sump, which acts as.a crucible for holding the permanent bath of molten lead, which latter may be introduced into the sump prior to feeding the ores, or may result from the reduction of the metallic lead from the stock operated. This bath acts a medium for collecting and holding in alloy as base bullion any gold or silver contained in the stock treated, and which is reduced to a metallic state directly in contact with the matte and bath in the combustion-chamber of the sump. As the volume of the bath increases by the reduction of lead in the stock treated, it is dipped from the lead-well E or allowed to overflow into molds, and is ready to ship as base bullion; or it may be run over a series of refining-plates and the precious metals separated from the base or lead bullion.
A very important feature of my invention is the molten matte or blanket contained in the sump above'the lead. Thisblanket or matte is formed automatically from the various reagents .fed with or found in the ores, and when once formed is permanent, its volume being sustained from the ores fed to the furnace, and any excess or surplus flowing off by the matte tap-hole, which is continuously open.
As before stated, the lead in the sump is automatically maintained at the proper level, and the blanket or matte is also automatically maintained, and thereby the lead is always properly covered by the matte, preventing scorification, and the slag freely flows off at the open slag-hole.
By arranging the furnaces as above de scribed the heat and flames from the fuel used, which may be of any desired character, are carried from the fire-boxes through the funnel -shaped throats into the combustion chamber, where they meet, being concentrated upon the smeltingpoint, and crossing each other in the sump they produce a sort of rotary flame, which is practically confined within the sump-arch above the blanket, and I am thereby enabled to utilize the greatest amount of heat and at the most effectual point.
Another feature of my invention consists in using an exhaust or suction blower instead of a blast-blower, and by this means, while Iain enabled to keep up the requisite amount of draft for the furnaces, the blanket or matte is not seriously disturbed or broken, as when the blast is used, and scorifieation and loss of the lead is prevented. Moreover, on account of the arrangement of the furnaces and sumparch as above indicated, I am enabled to draw the waste products of combustion and theheat through the expansion-chamber around the ore-conveyer more in the form of heated gases, as very little, if any, flame escapes from the sump-arch. This I find is very advantageous in reducing or desulphurizing them in the conveyer. \Vhere fluxes are necessary I mix them with the ores in the conveyer, and thereby avoid the necessity of feeding them separately to the reducing-point. The hole P in the top of the sump-arch enables me to feed rich stock-such as the tellurides, chlorides, Ste-without loss directly into the lead bath.
While I do not desire to limit myself to the precise details and construction set forth, as they may be varied without departing from the spirit of my invention, I have found the above-described arrangement forms a practical smelter of great capacity and applicable to the economical and complete reduction of all ores carrying precious metals, and producing the same in the form of base or lead bullion.
I am aware ore has been fed through a cylinder, where it was roasted in contact with hot air to charge it with oxygen, and then fed into another cylinder and roasted in direct contact with a flame, the sulphur being largely consumed and fluxes being added therein, and
ICC
then fed to the reducing-chamber, where the metals are precipitated in their order of gravitation, and I make no claim thereto.
Having thus described my invention, what I claim is 1. The process of smelting ores, substantially as herein set forth, which consists in gradually feeding the ores through a conveyer, subj ecting them therein to a temperature sufficient to desulphurize and reduce them to a semi-liquid state by the action of hot air, and concentrating the flames and heat from several sources directly upon the semi-liquid mass.
2. The combination,with a sump having an arched top or dome, of a series of fire-boxes, constructed and arranged substantially as described, and inclined concentrating-passages leading from the boxes to the interior of the sump, whereby the flames may be concentrated and confined in the sump, as and for the purposes described.
3. The combinatiomwith a sump, of an orcconveyer consisting of a tube having a suitable hopper and a screw-conveying rod and a series of perforations in the tube, the whole being arranged in the exhaust smoke-chamber leading from the sump, whereby the ores are desulphurized and delivered directly at the smelting-point in a liquid or semi-liquid state, substantially as described.
4. The combinatiomwith a sump having an arched top or dome containing a lead bath and metallic matte, of a series of fire-boxes located at one side of the sump, having inclined passages adapted to concentrate the flames and heat at the mouth of the conveyer, and a conveyer adapted to deliver the ore into the concentrated flames and heat, substantially as described.
5. The combination, with an arched sump containing a lead bath and a metallic matte,
and provided with means for maintaining the same at a constant level, of a series of fireboxes at one side of the sump, arranged to concentrate the heat and flames, an exhaust smoke-chamber at another side, and a conveyer located in said chamber, the arrangement being such that the flames and heat pass into the sump, are concentrated at the smelting-point without scorifying the lead bath, and are drawn through the exhaust-chamber, heating the ore in the conveyer, substantially as described.
6. The combination, with a sump and .fireboxes connected therewith, arranged to concentrate the flames and heat in the sump, of a smoke or dust chamber containing an oreconveyer, a condensing chamber connected therewith, an exhausting apparatus connected with the condensing-chamber, whereby the flames and heat are drawn into the sump and concentrated, and the products of combustion are drawn through the chambers, and means for supplying water to the condensingcham ber, as and for the purpose set forth.
7. The combination,with the sump contain ing a lead bath and a metallic blanket, of fire-boxes connected to said sump and a sumparch having an opening at the top and an oreconveyer located in the smoke-chamber,whereby the ordinary ores may be conveyed to the sump in a semi-liquid state, and the rich ores may be dropped directly into the sump at the smelting-point, substantially as described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
MATHEWV DAUSON BRETT.
Witnesses:
W'ILLIAM M. BROOKE, MEREDITH B. OAMPLIN.
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US320908A true US320908A (en) | 1885-06-30 |
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US320908D Expired - Lifetime US320908A (en) | Fotjeth to d estaing s |
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