US246690A - Reducing ores - Google Patents
Reducing ores Download PDFInfo
- Publication number
- US246690A US246690A US246690DA US246690A US 246690 A US246690 A US 246690A US 246690D A US246690D A US 246690DA US 246690 A US246690 A US 246690A
- Authority
- US
- United States
- Prior art keywords
- chamber
- ore
- reducing
- tube
- air
- 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
- 238000002485 combustion reaction Methods 0.000 description 16
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 150000002739 metals Chemical class 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 230000001590 oxidative Effects 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- 210000003800 Pharynx Anatomy 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 2
- 229910052787 antimony Inorganic materials 0.000 description 2
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000000725 suspension 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
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/20—Details, accessories, or equipment peculiar to rotary-drum furnaces
- F27B7/2016—Arrangements of preheating devices for the charge
- F27B7/2025—Arrangements of preheating devices for the charge consisting of a single string of cyclones
- F27B7/2033—Arrangements of preheating devices for the charge consisting of a single string of cyclones with means for precalcining the raw material
Definitions
- My invention relates to an improved process and furnace for volaiilizing and oxidizing ores, especially such as contain a large proportion of gold and silver. It is more particularly an improvement in the class of furnaces in which the ore, when broken up or in a comminuted state, is held in suspension or kept in constant circulation by means of ajet ofair, gas, or steam while being acted on by heat, as illustrated in Patent No. 212,508, granted to me February 2, 1879.
- the volatilization and oxidation of the baser elements-such as sulphur, arsenic, antimony, and iron-and their preparation for separation from the valuable metals, gold and silver are efiected very quickly and thorou ghly.
- A indicates the reducing-chamber of a furnace
- B the fuel-chamber
- G the tube through which the ore, in a state of more or less minute division, is'carried into the chamber A or else circulated through the latter in continuous round, as" hereinafter described.
- D is the smaller tube, through which air, steam, or other gas is forced to induce a current or circulation of ore.
- the ore-chamber A may be constructed of firebrick and have any desired capacity.
- the fuel-chamber B is connected with the red ucing-chamber by a narrow funnel-shaped throat or passage, E, whose mouth or widest end opens into the fuel-chamber.
- the nozzle or discharge end of tube 0 is located in the passage E and directed toward the reduction-chamber A.
- the nozzle of pipe D enters the nozzle of tube 0, and is arranged in the same manner-4. e., directed toward the reducing-chamber.
- the other end of the pipe D is connected with a steam-gem erator, air-blowerfor pump, or other suitable foreign apparatus. (Not shown.)
- the jet or current of steam or air proceeding from the pipe D will induce a current of ore through tube 0. It will also induce a current of products of. combustion and airfrom and through the fuel-chamber B.
- the flame and heated products of combustion will impinge on the particles of ore entering passage 1) from pipe 0, and together they will enter the chamber A, wherein the volatilization and oxidation begun in the passage D will be continued and perfected.
- ' I may introduce the crushed or pulverized ore into tube 0 through a hopper, If, as shown, or any other preferred medium.
- I connect the lower end of tube (3 with the base of chamber A, as shown, thus forming a continuous passage; or I may simply employ the tube alone, giving it a circular or other form, and arranging it in a furnace 'or over a grate, and directing the ore and blastintothe same in asuitable manner, and providing, also, for discharge of the metal.
- the air to support combustion and produce oxidation is induced or drawn into the fuel-chamber, and the products of combustion and ore mingled therewith are also induced and forced into the reducing-chamber by one and the same means, and the result effectedis complete and thorough volatilization and oxidation of the baser elements and preparation ot' the samefor elimination from the more valuable metalor metals in a very short time with the least expenditure of fuel and labor.
- the difl'used condition of the ore and the mode of applying the blast insure the action of the heat and air on each individual particle, and prevent the particles melting or cakin g together, so that the largest yield of the valuable metals is obtained at minimum cost.
- I showin the drawing a pipe, a, branching from tube 0, and having a flexible extension, I).
- This attachment is used for the purpose of feeding ore into the furnace from a heap or other body of the same.
- the cock 0 in pipe (t is opened and cock (1 in tube 0 closed when ore is to be fed in this manner. 1
- What I claim is 1.
- the process of reducing and oxidizing ores consisting in subjecting ore, when in a pulverized or comminuted state, to the action of a fire-blast, and driving or producing a continuous circulation through a continuous passage until the desired effect has been produced, as set forth.
Description
(No Model.)
0. E. ROBINSON.
REDUCING OEES No. 246,690. Patented Sept. 6,1881.
INVBNTOE:
. fizz; M KM ATTORNEYS.
WITNESSES N, PETERS. Plwlol-ilhogmphcr. washin mn. D. c.
NITED STATES PATENT OFFICE,
CHARLES E. ROBINSON, OF CHARLOTTE, NORTH CAROLINA.
REDUCING ORES.
SPECIFICATION forming part of Letters Patent No. 246,690, dated September 6, 1881.
Application filed September 3, 1880.
To all whom it may concern Be it known that I, CIiARLEs E. ROBINSON, of Charlotte, in the county of Mecklenburg and State of North Carolina, have invented a new and useful Improvenientin Reducing Ores; and I do hereby declare that the following is a full, clear, and exact description of the same.
My invention relates to an improved process and furnace for volaiilizing and oxidizing ores, especially such as contain a large proportion of gold and silver. It is more particularly an improvement in the class of furnaces in which the ore, when broken up or in a comminuted state, is held in suspension or kept in constant circulation by means of ajet ofair, gas, or steam while being acted on by heat, as illustrated in Patent No. 212,508, granted to me February 2, 1879. In the present case I efl'eet by an air or gas jet an induced feed of the pulverized ore into the reducing-chamber, and also an induced draft of air into the fuelchamber, and an induced blastor current of heated air and the products of combustion from the fuel-chamber into the reducing-chamber, the ore being mingled with and powerfully acted upon by the flame and heated products of combustion while on its way into the said chamber, and the ore and products of combustion being forced out of the chamber and again into the tube, so that they make a continuous round through a continuous passage.
In some cases I propose to dispense with the furnace proper and employ the tube alone, givingit acircular or other suitable form and arranging it over a grate or within a fire-chamber, so that heat may be applied to it externally; but, preferably, Iinduce ablast ot' the products of combustion vdirectly from the firechamber and force them through the tube mingled with the pulverized ore. In either way the volatilization and oxidation of the baser elements-such as sulphur, arsenic, antimony, and iron-and their preparation for separation from the valuable metals, gold and silver, are efiected very quickly and thorou ghly.
In the accompanying drawing I illustrate an apparatus for carrying out my process; but it may be modified in various ways and still involve the principles of my invention. The view given is a sectional elevation, and repre- (No model.)
sents a furnace, through the base ot' which steam or air may be injected,when desired, for the purpose of treating the ore, as described in my aforesaid patent.
' A indicates the reducing-chamber of a furnace; B, the fuel-chamber; and G, the tube through which the ore, in a state of more or less minute division, is'carried into the chamber A or else circulated through the latter in continuous round, as" hereinafter described. D is the smaller tube, through which air, steam, or other gas is forced to induce a current or circulation of ore. The ore-chamber A may be constructed of firebrick and have any desired capacity. The fuel-chamber B is connected with the red ucing-chamber by a narrow funnel-shaped throat or passage, E, whose mouth or widest end opens into the fuel-chamber. The nozzle or discharge end of tube 0 is located in the passage E and directed toward the reduction-chamber A. The nozzle of pipe D enters the nozzle of tube 0, and is arranged in the same manner-4. e., directed toward the reducing-chamber. The other end of the pipe D is connected with a steam-gem erator, air-blowerfor pump, or other suitable foreign apparatus. (Not shown.) The jet or current of steam or air proceeding from the pipe D will induce a current of ore through tube 0. It will also induce a current of products of. combustion and airfrom and through the fuel-chamber B. The flame and heated products of combustion will impinge on the particles of ore entering passage 1) from pipe 0, and together they will enter the chamber A, wherein the volatilization and oxidation begun in the passage D will be continued and perfected.
' I may introduce the crushed or pulverized ore into tube 0 through a hopper, If, as shown, or any other preferred medium.
I connect the lower end of tube (3 with the base of chamber A, as shown, thus forming a continuous passage; or I may simply employ the tube alone, giving it a circular or other form, and arranging it in a furnace 'or over a grate, and directing the ore and blastintothe same in asuitable manner, and providing, also, for discharge of the metal. For many purposes I prefer this latter method and arrangement as involving certain advantages, more particularly in respect to compactness and economy of construction of the furnace as a whole, and to economy in working the same. In either case the air to support combustion and produce oxidation is induced or drawn into the fuel-chamber, and the products of combustion and ore mingled therewith are also induced and forced into the reducing-chamber by one and the same means, and the result effectedis complete and thorough volatilization and oxidation of the baser elements and preparation ot' the samefor elimination from the more valuable metalor metals in a very short time with the least expenditure of fuel and labor. The difl'used condition of the ore and the mode of applying the blast insure the action of the heat and air on each individual particle, and prevent the particles melting or cakin g together, so that the largest yield of the valuable metals is obtained at minimum cost.
In addition to the features before described, I showin the drawing a pipe, a, branching from tube 0, and having a flexible extension, I). This attachment is used for the purpose of feeding ore into the furnace from a heap or other body of the same. The cock 0 in pipe (t is opened and cock (1 in tube 0 closed when ore is to be fed in this manner. 1
What I claim is 1. The process of reducing and oxidizing ores, consisting in subjecting ore, when in a pulverized or comminuted state, to the action of a fire-blast, and driving or producing a continuous circulation through a continuous passage until the desired effect has been produced, as set forth.
2. The combination, with an ore-reducing chamber and furnace-chamber, of an ore-conducting pipe, arranged with one of its open ends in communication with the lower portion of the reducing'chambers and the other in the mouth of the fire-chamber, and a steam, air, or gas injecting pipe which is connected with the orepipe, substantially as shown and described, whereby the' steam or gas jet or current produces an induced fire-blast and creates and maintains a circulation of the pulverized ore through a continuous passage, as set forth.
The above specification of my invention signed by me this 28th day of August, 1880.
CHAS. E. ROBINSON.
Witnesses:
CHAS. A. Pn'r'rrr, SoLoN O. KEMON, Amos W. HART.
Publications (1)
Publication Number | Publication Date |
---|---|
US246690A true US246690A (en) | 1881-09-06 |
Family
ID=2316015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US246690D Expired - Lifetime US246690A (en) | Reducing ores |
Country Status (1)
Country | Link |
---|---|
US (1) | US246690A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2496203A (en) * | 1948-05-10 | 1950-01-31 | Cudahy Packing Company | Beneficiation of volcanic ash |
US4378209A (en) * | 1981-08-28 | 1983-03-29 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Gas levitator having fixed levitation node for containerless processing |
US6461400B1 (en) | 2000-04-12 | 2002-10-08 | Art J. Parker | Process for extracting quantities of precious metals |
-
0
- US US246690D patent/US246690A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2496203A (en) * | 1948-05-10 | 1950-01-31 | Cudahy Packing Company | Beneficiation of volcanic ash |
US4378209A (en) * | 1981-08-28 | 1983-03-29 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Gas levitator having fixed levitation node for containerless processing |
US6461400B1 (en) | 2000-04-12 | 2002-10-08 | Art J. Parker | Process for extracting quantities of precious metals |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US246690A (en) | Reducing ores | |
US212508A (en) | Improvement in furnaces for roasting ores | |
US4526A (en) | Improvement in the mode o | |
US303456A (en) | Furnace for desulphurizing and oxidizing ores | |
US290115A (en) | eussell | |
US165561A (en) | Improvement in steam or gas and air blast pipes for furnaces | |
US198413A (en) | Improvement in roasting ores | |
US198283A (en) | Improvement in shaft-furnaces for smelting tailings and condensing mercury | |
US160649A (en) | Improvement in ore-roasting furnaces | |
US216561A (en) | Improvement in smelting fine or dust ores | |
US582587A (en) | Apparatus for utilizing heat of furnace products | |
US275272A (en) | Roasting and reducing furnace for gold and silver ores | |
US512235A (en) | Process of and apparatus for roasting ores | |
US226692A (en) | Eilby p | |
US774304A (en) | Metallurgical process. | |
US287945A (en) | Ore-reducing furnace | |
US116903A (en) | Improvement in treatment of ores by means of fuel, chemicals, and fluxes | |
US232537A (en) | Furnace for roasting and reducing ores | |
US1030152A (en) | Open-hearth process of refining steel. | |
US117360A (en) | Improvement in furnaces for roasting ores | |
US215971A (en) | Improvement in desulphurizers | |
US186975A (en) | Improvement in furnaces and processes for manufacturing iron and steel | |
US207065A (en) | Improvement in ore roasting and desulphurizing furnaces | |
USRE4898E (en) | Improvement in processes of roasting, burning | |
US117363A (en) | Improvement in desulphurizing and treating ores |