US495550A - Process of concentrating zinc-bearing sulphide ores - Google Patents
Process of concentrating zinc-bearing sulphide ores Download PDFInfo
- Publication number
- US495550A US495550A US495550DA US495550A US 495550 A US495550 A US 495550A US 495550D A US495550D A US 495550DA US 495550 A US495550 A US 495550A
- Authority
- US
- United States
- Prior art keywords
- zinc
- iron
- per cent
- lead
- magnetic
- 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
- 229910052725 zinc Inorganic materials 0.000 title description 25
- 239000011701 zinc Substances 0.000 title description 25
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical group [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 22
- 238000000034 method Methods 0.000 title description 12
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 title description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 50
- 229910052742 iron Inorganic materials 0.000 description 26
- 239000011133 lead Substances 0.000 description 22
- 239000000047 product Substances 0.000 description 16
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 10
- 239000005864 Sulphur Substances 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000003723 Smelting Methods 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 5
- UCNNJGDEJXIUCC-UHFFFAOYSA-L hydroxy(oxo)iron;iron Chemical compound [Fe].O[Fe]=O.O[Fe]=O UCNNJGDEJXIUCC-UHFFFAOYSA-L 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 239000004332 silver Substances 0.000 description 5
- 230000008030 elimination Effects 0.000 description 4
- 238000003379 elimination reaction Methods 0.000 description 4
- 239000006148 magnetic separator Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 229910052952 pyrrhotite Inorganic materials 0.000 description 2
- 239000000696 magnetic material Substances 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052950 sphalerite Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- WGPCGCOKHWGKJJ-UHFFFAOYSA-N sulfanylidenezinc Chemical compound [Zn]=S WGPCGCOKHWGKJJ-UHFFFAOYSA-N 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 229910052984 zinc sulfide Inorganic materials 0.000 description 1
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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
Definitions
- the usual practice for obtaining the precious metals from sulphide ores bearing zinc, lead, 850., and containing silver, &c. consistsin first concentrating the ores (which is done at the mines) for the removal of the lead and iron, and secondly, the roasting of the ores as a preliminary to smelting (which is done at the works) for the elimination of the sulphur; and in said roasting process, when the sulphur is nearly eliminated, the heat is so increased as to fuse and cake the lead, and form a mass for the smelting furnace.
- My invention has therefore for its object, first to facilitate the concentration of refractory zinc-bearing sulphide ores, such as are found in Colorado and elsewhere; and second, the production of a concentrate cornparatively low in zinc, and therefore of greatly increased value to the smelter.
- the zinc bearing sulphide ores referred to, and to which my invention more especially applies consist of zinc, iron, lead, silver, silica, and other foreign substances in small quantities.
- the zinc in such ores is known as sphalerite or zinc in the form of zinc blende, and the iron occurs generally in two forms, about ninetyeight (98%) per cent.
- the roasting of the ore should be so conducted, that the final stage, or that wherein the sulphur is aimost-or entirelydriven off, shall be conducted without materially increasing the heat of the furnace and in the presence of areducing atmosphere, whereby a portion of the contained lead is precipitated or deposited on the iron and can be eliminated therewith in the subsequent step of magnetic separation or elimination of the iron, and this particular method of roastin g the ore for the purposes of separation and concentration, forms in itself a subordinate, but valuable, feature of my invention, as, where more than five per cent.(5%) of lead is present with the iron product, the lead is allowed and paid for, and not otherwise.
- This product is then passed through a magnetic separator, and I obtain two products as follows: The first which I term magnetic and which constitutes about forty six (46%) per cent. of the mass, contains 11 OZ Ag17.3% Pb1.3% sio,-45.5% Fe 7.5% Zn.
- This second or non-magnetic product is then concentrated by any of the well known methods, and as the specific gravity of lead (11.36) is so much greater than that of zinc (7.13) the lead is readily separated. As a result of this concentration I obtain two products: The first which I term lead concentrate will contain 22.2 oz Ag-71% Pb0.5% SiO 9% Fe 7% Zn,
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
UNTTED STATES ATENT Trice,
PROCESS OF CONCENTRATING ZINC-BEARING SULPHIDE ORES.
SPECIFICATION forming part of Letters Patent No. 495,550, dated April 18,1893.
Application filed November 25, 1891. $erial No. 413,084. (No specimens.)
To all whom it may concern:
Be itknown that I, GUsTAvn M. GOUYARD, a citizen of the United States, residing at Denver,in the county of Arapahoe and State of Colorado, have invented certain new and useful Improvements in Processes'of Concentrating Zinc-Bearing Sulphide Ores; and I hereby declare the following to be a full, clear, and exact description of the same, such as will enable others skilled in the art to which it appertains to apply the invention.
As is well understood, the usual practice for obtaining the precious metals from sulphide ores bearing zinc, lead, 850., and containing silver, &c., consistsin first concentrating the ores (which is done at the mines) for the removal of the lead and iron, and secondly, the roasting of the ores as a preliminary to smelting (which is done at the works) for the elimination of the sulphur; and in said roasting process, when the sulphur is nearly eliminated, the heat is so increased as to fuse and cake the lead, and form a mass for the smelting furnace. The close specific gravity of iron (7.78) and zinc (7.13) renders the concentration process a very delicate and difficult one to conduct cheaply on a commercial scale; and the presence of a very large per cent. of zinc in the concentrate, as delivered to the smelter, adds considerably to the cost of smelting.
My invention has therefore for its object, first to facilitate the concentration of refractory zinc-bearing sulphide ores, such as are found in Colorado and elsewhere; and second, the production of a concentrate cornparatively low in zinc, and therefore of greatly increased value to the smelter. The zinc bearing sulphide ores referred to, and to which my invention more especially applies, consist of zinc, iron, lead, silver, silica, and other foreign substances in small quantities. The zinc in such ores is known as sphalerite or zinc in the form of zinc blende, and the iron occurs generally in two forms, about ninetyeight (98%) per cent. of the whole being iron pyrites (FeS and the balance (two per cent.) being pyrrhotite (Fe S My invention, therefore, generally stated, consists in sujecting zinc bearing sulphides, of the class above stated, or their equivalents to the following steps: first so roasting the ore as to obtain a magnetic oxide of iron,sec-= ondly, passing the ore thus roasted, through a magnetic separator for the elimination of the magnetic oxide, and fially, concentrating the tailings of the magnetic separator for the elimination of zinc. In order, however, to obtain the best results, the roasting of the ore should be so conducted, that the final stage, or that wherein the sulphur is aimost-or entirelydriven off, shall be conducted without materially increasing the heat of the furnace and in the presence of areducing atmosphere, whereby a portion of the contained lead is precipitated or deposited on the iron and can be eliminated therewith in the subsequent step of magnetic separation or elimination of the iron, and this particular method of roastin g the ore for the purposes of separation and concentration, forms in itself a subordinate, but valuable, feature of my invention, as, where more than five per cent.(5%) of lead is present with the iron product, the lead is allowed and paid for, and not otherwise.
As mines and smelters almost universally compute by the ton of two thousand (2,000) pounds, therefore, wherever hereinafter a percentage is specified, it is to be understood as a percentage of such a ton of oreor product as the case may be, and wherever I refer to weight (as for instance eleven and one-half ounces silver) it is such an amount to the ton of ore or product as the case may be.
I will now proceed to describe my invention in detail. I take an ore, which for the purposes of illustration may be said to contain thirty six per cent. sulphur, nineteen per cent. lead, twenty one and three tenths per cent. iron, seventeen and three tenths per cent. zinc, one per cent. silica, and eleven and one half ounces silver:
This ore I first roast at a low heat, or as is now commonly done at the smelting works, until the sulphur is nearly eliminated, and at this stage of the roasting process, instead of raising the heat as is done at the smelting works, I maintain the same low steady heat as near as possible, and also at this stage produce in the furnace a reducing atmosphere, adding fine pulverized coal in order to convert the two forms of iron, viz: Iron pyrites (FeS and pyrrhotite (Fe S into a single form.(Fe O or a magnetic oxide of iron. Incidental to the operation of roasting as thus conducted, there is deposited or precipitated upon the magnetic oxide a certain per cent. of the contained lead,which can be eliminated with the iron in a subsequent stage of the process. As a result of this first roasting step, I get a product containing five per cent. sulphur, twenty eight and one half per cent. lead, twenty five and eight tenths per cent. iron, sixteen and seven tenths per cent. zinc, one and two tenths per cent. silica, and fourteen ounces of silver.
(5% S28.5% Pb25.8% Fe--16.7% Zn 1.2% SiO 14@ oz Ag.)
This product is then passed through a magnetic separator, and I obtain two products as follows: The first which I term magnetic and which constitutes about forty six (46%) per cent. of the mass, contains 11 OZ Ag17.3% Pb1.3% sio,-45.5% Fe 7.5% Zn.
The second which I term non-magnetic which constitutes about fifty four (54%) per cent, and which contains 15.6 oz Ag-37% Pb1.4% sio,-9.5% Fo- It will be noted that the first or magnetic product, while it runs high in iron (45.5 per cent.) runs very low in zinc (7.5 per cent); and that the second or non-magnetic product runs low in iron (9.5 per cent.) and high in lead (37 per cent.) and zinc (24.8 per cent). This second or non-magnetic product is then concentrated by any of the well known methods, and as the specific gravity of lead (11.36) is so much greater than that of zinc (7.13) the lead is readily separated. As a result of this concentration I obtain two products: The first which I term lead concentrate will contain 22.2 oz Ag-71% Pb0.5% SiO 9% Fe 7% Zn,
while the second which I will term zinc concentrate, will contain 9 oz Ag3% Pb2% SiO 10% Fe- By the process hereinbefore described I obtain, as will be noted, first the magnetic product rich in iron ore; and second, the lead concentrate 22.2 oz Ag-'71% Pb-O.5% SiO 9% Ferich in lead; and in both, the zinc has been reduced to seven or eight (7% or 8%) per cent, and the sulphur to five (5%) per cent. or less; a very desirable feature, as the smelters give a better price for products low in zinc and which contains little or no sulphur.
Having thus described my invention, what I claim, and desire to secure by Letters Patent, is-
1. As a step in the concentration of zinc bearing sulphide ores of the class specified, the process herein described which consists in subjecting the ore at the final stage of roasting and when the sulphur is nearly or entirely eliminated to a low heat in the presence of a reducing atmosphere which reduces the iron in the ore from its two forms (FeS and Fe S to the common form of magnetic oxide (Fe O and precipitates lead thereon, then separating magnetically the roasted product whereby is obtained a magnetic product containing a large percentage of iron oxide (Fe O and lead, and a non-magnetic product which is concentrated; substantially as and for the purpose specified.
2. The process of separating lead and iron from sulphide ores carrying lead, iron, zinc, and sulphur which consists in crushing the ore, roasting the ore, and mixing at the last stage of roasting a small percentage of fine pulverized coal which renders the iron in the ore magnetic and precipitates the lead on the iron, and then separating magnetically the magnetic material which consists of the iron and lead precipitated thereon, from the nonmagnetic parts of the ore, and thus obtaining a valuable magnetic product substantially as described.
In testimony whereof I affix my signature, in presence of two witnesses, this 21st day of November, 1891.
GUSTAVE M. GOUYARD.
WVitnesses:
ALMARIN B. PAUL, J. H. CRAGG.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US495550A true US495550A (en) | 1893-04-18 |
Family
ID=2564388
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US495550D Expired - Lifetime US495550A (en) | Process of concentrating zinc-bearing sulphide ores |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US495550A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2991171A (en) * | 1958-07-02 | 1961-07-04 | American Metal Climax Inc | Germanium concentration and production |
-
0
- US US495550D patent/US495550A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2991171A (en) * | 1958-07-02 | 1961-07-04 | American Metal Climax Inc | Germanium concentration and production |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Anderson | The metallurgy of antimony | |
| EP0128887A1 (en) | A method for processing copper smelting materials and the like containing high percentages of arsenic and/or antimony | |
| CN108823425A (en) | A kind of difficult-treating gold mine fused-extracting enrichment Method for extracting gold | |
| US4372782A (en) | Recovery of lead and silver from minerals and process residues | |
| US495550A (en) | Process of concentrating zinc-bearing sulphide ores | |
| US4521245A (en) | Method of processing sulphide copper- and/or sulphide copper-zinc concentrates | |
| US3174848A (en) | Process for treating high antimonybearing gold ores | |
| EP0042702B1 (en) | Process for the recovery of lead and silver from minerals and process residues | |
| US3463630A (en) | Process for producing zinc and related materials | |
| US2816022A (en) | Smelting of lead-containing ores | |
| CN108823426A (en) | A kind of method of rich golden iron sulfonium melting back extraction Concentration of Gold | |
| Clevenger et al. | The treatment of manganese-silver ores | |
| US722809A (en) | Method of treating ores. | |
| US4789529A (en) | Recovery of zinc from zinc bearing sulphidic ores and concentrates by controlled oxidation roasting | |
| US3942976A (en) | Metal recovery process | |
| Dosmukhamedov et al. | Behavior of Сu, Zn, Pb, As compounds during copper-zinc concentrate and matte comelting in converters | |
| EP0195650A2 (en) | Recovery of zinc from zinc-bearing sulphidic ores and concentrates by controlled oxidation roasting | |
| US2639220A (en) | Method of making copper sulfate | |
| US3155492A (en) | Metallurigical process | |
| US249981A (en) | Eichaed peaege | |
| US1098443A (en) | Process for separating copper from nickel and cobalt. | |
| US4274868A (en) | Recovery of tin from ores or other materials | |
| US1518626A (en) | Treatment of copper-lead matte | |
| US1789932A (en) | Process of extracting metal values from ores | |
| US1801105A (en) | Process of sulphide ore treatment |