US385235A - Aethttb cbossman bbadley - Google Patents
Aethttb cbossman bbadley Download PDFInfo
- Publication number
- US385235A US385235A US385235DA US385235A US 385235 A US385235 A US 385235A US 385235D A US385235D A US 385235DA US 385235 A US385235 A US 385235A
- Authority
- US
- United States
- Prior art keywords
- metal
- chamber
- air
- oxide
- oxidizing
- 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
- 239000002184 metal Substances 0.000 description 50
- 229910052751 metal Inorganic materials 0.000 description 50
- 238000000034 method Methods 0.000 description 24
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 239000004744 fabric Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000003345 natural gas Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000001590 oxidative Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229910001111 Fine metal Inorganic materials 0.000 description 2
- 241000005139 Lycium andersonii Species 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000002817 coal dust Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 239000012255 powdered metal Substances 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G21/00—Compounds of lead
- C01G21/02—Oxides
Definitions
- Figure l of said drawings represents a central vertical section of said furnace, and Fig. 2 represents a transverse section of the same at one of the sets of gas-burners.
- thefmetal in a comininuted condition is subjected to the action of agas-ame-such as that produced from natural gas (or gas from coal)-burned with an excess of air, the mixed atmosphere of fiame and air being at a temperature sufficient to burn the comminuted metal.
- agas-ame such as that produced from natural gas (or gas from coal)-burned with an excess of air, the mixed atmosphere of fiame and air being at a temperature sufficient to burn the comminuted metal.
- the resultant oxide is then collected in a pulverulent condition.
- the oxidizingchamber A is upright. At the upper end of this chamber there is an escape-passage, a2, through which the spent products of the combustion of the gas and the pulverulent oxide carried with them can pass to a dust-collector, and it is itted near its lower end with an inlet-passage, a, through which air may, if necessary, be introduced.
- the lower end of the oxidizing-chamber terminates, preferably, in a receptacle, a3, to receive any unoxidized metal.
- a charger D, by means of which the metal to be oxidized is fed to the inclosed oxidizingchamber, and the neck ot' this chargeris pref; erably fitted with a sliding gate or valve, d, by means of which the supply of metal can be regulated.
- the neck d of the charger is preferably extended into the oxidizing-chamber sufficiently to have the lower end of the neck below the orifice of the escape-pipe a2,- and, as it is desirable to prevent the metal when previously comminuted from melting in the neck ot' the charger, the extension of the neck into the said chamber is surrounded by a water-jacket, d2, through which a current of water is caused to pass, the water being supplied by means of a water-supply pipe, e, and the warm water being permitted to escape through an escape-water pipe, e.
- the gas-flame may be made directly in the oxidizing-chamber by means of' burners inserted in its walls, or may be made in a preliminary combustioachamber and introduced into the oxidizing-chamber through one or more of the inlet-passages a, above described.
- the oxidizingchamber A is tted with burners c, through which natural gas is introduced, these gas-burners being of the construction of the well ⁇ known Bunsen burner, so that the gas is mixed with air.
- the action of the Bunsen burners introduces an excess of air and creates a strong draft upward through the oxidizing-chamber, and whatever additional air may be required to thoroughly oxidize the metal is admitted through one or more orifices, a, beneath the gasburners, a forced current being introduced if a current strong enough to make the operationpractically successfulis not obtained by draft.
- the gasburners must be of sufficient capacity to heat the atmosphere within the oxidizing-chamber and the current of air passing Vthrough that' chamber to the requisite temperature for the rapid oxidation of the metal.
- the dust-collector may be one of the varieties mentioned in my said previous application.
- the atmosphere within the oxidizing-chamber by means of the gas-flame to a temperature somewhat higher than that at which the metal rlhe comminuted metal to be oxidized, which may be lead, is placed into the charger D, and is permitted (by opening the gate d) to flow into the oxidizing-chamber.
- rlhe comminuted metal falls through the said chamber in a shower, so that the atmosphere therein has free access to its particles, which are acted upon simultaneously by heat and the current of air. Consequently the metal burns or oxidizes rapidly, and is converted mainly into a pulverulent oxide.
- the pulverulent oxide produced cannot escape from the current, but is carried off by the current and is deposited in the dust-collector, whence it may be removed through the doorways or openings provided forthe purpose.
- a bag dust collector be used, its bags must be made of cloth porous to air, so that the air will filter through the cloth of the bags, leaving the oxide within them to be withdrawn at intervals, as is customary with this class of dust-collectors.
- Such larger particles of the com minuted metal as are not fully oxidized drop into the receiver a at the lower end of the Aoxidizing-chamber, and may be removed at intervals through a doorway provided for that purpose.
- the oxidizing-chamber should be formed of a material that Will withstand the heat, it having been constructed by me of fire-brick material, and it should, if necessary, be lined or coated on its interior with some material that Will not melt readily when acted upon by the metallic oxide.
- lead is the metal that is oxidized
- the com minuted metal is subjected directly to the action of an inclosed gasflame, with excess of air in a current. Consequently the high temperature required can be readily maintained without the external heating of the oxidizingchamber, and the oxidation is rapid. Moreover, as the gas-flame is inclosed, the diffusion of the oxide in air is avoided, and the. oxide may be collected by I the dust-collector.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
(Mmmm.) l
A. C. BRADLEY. PROCESS 0F MANUFACTURING OXIDE OPIRON.
No. 385,235. PanentedJu-n@ 26, 1888.
` Nrrnn STATES ARTHUR onossMAN BRADLEY, on BROOKLYN, New YORK.n
PROCESS OFIVIANUFACTURING OXIDE OF IRON.
SPECIFICATION forming part of Letters Patent No. 385,235, dated June 26, 1888.
Application filed August 12, |887. Serial No. 246,796. (No model.)
To a/ZZ whom, it may concern.-
Be it known that I, ARTHUR CRossMAN BRADLEY, of Brooklyn, inthe county of Kings and State of New York, have made an invention of a new and useful Process of Manufacturing the Oxides of Rcadily-Oxidiza'ble Metals for Paints and for other Purposes; and I do hereby declare that the following, in connection with the accompanying drawings, is a full, clear, and exact description and specication of the same.
In an application for a patent, the specification of which is dated the 17th day of February, A. D. 1887, the serial number of which 1" is 228,290, I have described and claimed a process of manufacturing the oxides of metals,
and the invention which constitutes the subject-matter of this patent is a modification of the said process involving the invention of that application but restricted to a special mode of' treatmentof the metals to be oxidized, as set forth in the claims at the close of this specification.
In order that this invention may be fully understood, I have represented in the aecompanying drawings and will proceed to describe the form of afurnace which I prefer to use in practicing my said invention.
Figure l of said drawings represents a central vertical section of said furnace, and Fig. 2 represents a transverse section of the same at one of the sets of gas-burners.
In practicing my invention, thefmetal in a comininuted condition is subjected to the action of agas-ame-such as that produced from natural gas (or gas from coal)-burned with an excess of air, the mixed atmosphere of fiame and air being at a temperature sufficient to burn the comminuted metal. The resultant oxide is then collected in a pulverulent condition.
In the form of oxidizingfurnace represented in the drawings the oxidizingchamber A is upright. At the upper end of this chamber there is an escape-passage, a2, through which the spent products of the combustion of the gas and the pulverulent oxide carried with them can pass to a dust-collector, and it is itted near its lower end with an inlet-passage, a, through which air may, if necessary, be introduced. The lower end of the oxidizing-chamber terminates, preferably, in a receptacle, a3, to receive any unoxidized metal. At the upper end of the oxidizing-chamber there is a charger, D, by means of which the metal to be oxidized is fed to the inclosed oxidizingchamber, and the neck ot' this chargeris pref; erably fitted with a sliding gate or valve, d, by means of which the supply of metal can be regulated. The neck d of the charger is preferably extended into the oxidizing-chamber sufficiently to have the lower end of the neck below the orifice of the escape-pipe a2,- and, as it is desirable to prevent the metal when previously comminuted from melting in the neck ot' the charger, the extension of the neck into the said chamber is surrounded by a water-jacket, d2, through which a current of water is caused to pass, the water being supplied by means of a water-supply pipe, e, and the warm water being permitted to escape through an escape-water pipe, e.
The gas-flame may be made directly in the oxidizing-chamber by means of' burners inserted in its walls, or may be made in a preliminary combustioachamber and introduced into the oxidizing-chamber through one or more of the inlet-passages a, above described.
In the furnace represented in the drawings the oxidizingchamber A is tted with burners c, through which natural gas is introduced, these gas-burners being of the construction of the well` known Bunsen burner, so that the gas is mixed with air. The action of the Bunsen burners introduces an excess of air and creates a strong draft upward through the oxidizing-chamber, and whatever additional air may be required to thoroughly oxidize the metal is admitted through one or more orifices, a, beneath the gasburners, a forced current being introduced if a current strong enough to make the operationpractically successfulis not obtained by draft. The gasburners must be of sufficient capacity to heat the atmosphere within the oxidizing-chamber and the current of air passing Vthrough that' chamber to the requisite temperature for the rapid oxidation of the metal.
The dust-collector may be one of the varieties mentioned in my said previous application.
gas-furnace above described I prefer to heat In practicing my invention with the IOO .to be treated will burn in air.
the atmosphere within the oxidizing-chamber by means of the gas-flame to a temperature somewhat higher than that at which the metal rlhe comminuted metal to be oxidized, which may be lead, is placed into the charger D, and is permitted (by opening the gate d) to flow into the oxidizing-chamber. rlhe comminuted metal falls through the said chamber in a shower, so that the atmosphere therein has free access to its particles, which are acted upon simultaneously by heat and the current of air. Consequently the metal burns or oxidizes rapidly, and is converted mainly into a pulverulent oxide. As the current of hot airin which the metal is burned is inclosed or confined by the walls of the oxidizing-chamber, the pulverulent oxide produced cannot escape from the current, but is carried off by the current and is deposited in the dust-collector, whence it may be removed through the doorways or openings provided forthe purpose. lf a bag dust collector be used, its bags must be made of cloth porous to air, so that the air will filter through the cloth of the bags, leaving the oxide within them to be withdrawn at intervals, as is customary with this class of dust-collectors. Such larger particles of the com minuted metal as are not fully oxidized drop into the receiver a at the lower end of the Aoxidizing-chamber, and may be removed at intervals through a doorway provided for that purpose.
The oxidizing-chamber should be formed of a material that Will withstand the heat, it having been constructed by me of fire-brick material, and it should, if necessary, be lined or coated on its interior with some material that Will not melt readily when acted upon by the metallic oxide. When lead is the metal that is oxidized, I have. found that it is expedient to line the inside of the oxidizingchamber with bone-ashes, which may be moistened and rammed in around a wooden former or core, which is subsequently withdrawn.
f In this process the com minuted metal is subjected directly to the action of an inclosed gasflame, with excess of air in a current. Consequently the high temperature required can be readily maintained without the external heating of the oxidizingchamber, and the oxidation is rapid. Moreover, as the gas-flame is inclosed, the diffusion of the oxide in air is avoided, and the. oxide may be collected by I the dust-collector.
'My process therefore differs from the preceding process of heating fine metal in the open air in the respect that in such case the metal` was not subjected to an inclosed gas-dame. It also differs from the manufacture of a metallic oxide by burning a mixture of powdered metal with coal-dust in the respect that the comminuted metal is by my invention subjected free of earthy matter directly to the gas-flame.` It also differs from the process of roasting ores in fiame in the respect that according to my process the material operated upon is already in the metallic condition and is free from mixture with earthy matter, which, when ores are treated, produces a mixed productof earthy and metallic matter, and also in the respect that the comminuted metal itself, as distinguished from a compound of it, is directly operated upon by the heat and the oxidizing agency of the air.
I do not claim in this patent the process of oxidizing comminuted metal and collecting the pulverulent oxide, as claimed in my previous application, dated the 17th day of February, A. D. 1887, the serial number of which is 228,290, or the process` clai med in my application No. 228,496, file'dFebruary 23, 1887.
l claim as my invention in this patent- 1. The process, substantially as before set forth,of manufacturing an oxide directly from a metal,which consists in subjecting the metal, in a comminuted condition and free from earthy matter, directly to the action of an inclosed gas- Aflame,with an excess of highly-heated air and .in collecting the pulverulent oxide from said current.
2. The process, substantially as before set forth,of manufacturing an oxide directly from a metal, which consists in subjecting the comminuted metal free from'earthy matter in a shower direct-ly to the action of an inclosed gasiiame and heated air,and in collecting the pulverulent oxide from said current.
In witness whereof I have hereto set my hand this 8th day of August, A. D. 1887.
ARTHUR CR'OSSMAN BRADLEY.
Witnesses:
WALTER STABLER, Jas. E. WARNER.
it is hereby oertied that in Letters Patent No. 385,235, granted June 5 upon the application of Arth/ur Grossman Bradley, of Brooklyn, New York, th the invention was erroneously Written and printed Process of Manufaeturn of Iron, Whereas the said titleshould have been Written and printed Process 1 factoring Metallic Oxides,- and that the said Letters Patent should be read correction therein to make the same conform to the record of the casein th Ofoe.
Signed, oonntersigned, and sealed this 10th day of July, A. D. i888.
D. L. HAWKIE Assistant Secretary of the [SEAL] Gountersigned:
BENTON J. HALL,
Commissioner of Patents.
Publications (1)
Publication Number | Publication Date |
---|---|
US385235A true US385235A (en) | 1888-06-26 |
Family
ID=2454219
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US385235D Expired - Lifetime US385235A (en) | Aethttb cbossman bbadley |
Country Status (1)
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3450503A (en) * | 1964-11-12 | 1969-06-17 | Goldschmidt Ag Th | Apparatus for oxidizing lead |
US3963517A (en) * | 1973-06-01 | 1976-06-15 | Aktiebolaget Tudor | Process for the manufacture of lead storage battery electrodes and apparatus for carrying out the process |
-
0
- US US385235D patent/US385235A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3450503A (en) * | 1964-11-12 | 1969-06-17 | Goldschmidt Ag Th | Apparatus for oxidizing lead |
US3963517A (en) * | 1973-06-01 | 1976-06-15 | Aktiebolaget Tudor | Process for the manufacture of lead storage battery electrodes and apparatus for carrying out the process |
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