US420030A - Process of treating silver and zinc ores - Google Patents
Process of treating silver and zinc ores Download PDFInfo
- Publication number
- US420030A US420030A US420030DA US420030A US 420030 A US420030 A US 420030A US 420030D A US420030D A US 420030DA US 420030 A US420030 A US 420030A
- Authority
- US
- United States
- Prior art keywords
- zinc
- ore
- sulphur
- silver
- ores
- 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
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- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 48
- 229910052725 zinc Inorganic materials 0.000 title description 48
- 239000011701 zinc Substances 0.000 title description 48
- 238000000034 method Methods 0.000 title description 28
- 229910052709 silver Inorganic materials 0.000 title description 24
- 239000004332 silver Substances 0.000 title description 24
- 239000005864 Sulphur Substances 0.000 description 34
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 34
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 22
- 239000000446 fuel Substances 0.000 description 16
- 239000004215 Carbon black (E152) Substances 0.000 description 12
- 150000002430 hydrocarbons Chemical class 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000001117 sulphuric acid Substances 0.000 description 8
- 235000011149 sulphuric acid Nutrition 0.000 description 8
- 239000003517 fume Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 239000011133 lead Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- BWFPGXWASODCHM-UHFFFAOYSA-N Copper monosulfide Chemical compound [Cu]=S BWFPGXWASODCHM-UHFFFAOYSA-N 0.000 description 2
- 241000392035 Oreas Species 0.000 description 2
- 240000004713 Pisum sativum Species 0.000 description 2
- 235000010582 Pisum sativum Nutrition 0.000 description 2
- 241000876852 Scorias Species 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 2
- 239000003830 anthracite Substances 0.000 description 2
- 239000002802 bituminous coal Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000001066 destructive Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- MBMLMWLHJBBADN-UHFFFAOYSA-N iron-sulfur Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000001039 zinc pigment 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
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/003—Bath smelting or converting
- C22B15/0036—Bath smelting or converting in reverberatory furnaces
Definitions
- PETERS Fhnla-Uthcgrapl'vln Washinglum u c UNITED STATES ATENT FrIcE.
- This invention relates to the treatment of the so-called sulphuret ores, more particularly such ores as contain large quantities of zinc in the form of zinc sulphuret, together with more or less silver, lead, copper, dzc.
- the object of the present invention is to devise a method of treatment whereby the zinc may be carried off in the form of fume without taking with it any appreciable amount of silver, and the silver left behind in the slag to be again smelted by the usual methods.
- the invention is based on the factbelieved to be hitherto unknown that when ores containing silver and zinc are burned in the presence of an excess of sulphur the zinc escapes withouttaking with it any of the silver.
- the process consist-s, broadly, of mixingthe ore with ahydrocarbon fuel, adding an excess of sulphur in some suitable form if the ore does not contain an excess of sulphur, burning it in the presence of an air-blast forced uniformly through the mass from the under side thereof, and admitting air above the burning ore to destroy the sulphuric acid which would otherwise be given 05.
- an excess of sulphuris meantaquantity equal to or exceeding the amount of the zinc content.
- a fair example of the ores which it is designed to treatby this process would contain zinc, thirty per cent; lead, ten per cent; iron, ten per cent; sulphur, twenty per cent.; silica, thirty per cent. To this should be added sulphur enough to equal the amount of zinc contained in the oreas, for instance, fifty parts of iron and copper sulphide. If the ore contained sulphur equal to or greater in amount than the zinc, no sulphur would be added.
- I prefer to proceed as follows, viz: I take the raw ore and then crush it to a pea and grain size, and mix it with two-thirds,by weight, of finely-divided petroleum oils or residues, bituminous coal, saw-dust, or other flaming fuel. I then charge it into a furnace having a perforated hearth, in a shallow layer about four inches deep.
- the Wetherel hearth so called, with some modifications, is well suited to my process.
- the ore is burned in presence of an airblast, which is forced up through the perfo rated hearth, and a sufficient quantity of air.
- the zinc and lead, it any are present, are largely given oif in the form of fume, and may be collected in a bag-room or by other suitable means.
- Part of the sulphur unites with the copper, iron, silver, and gold, and forms a cinder or scoria, which retains all the non-volatile metals,wh ich may be subsequently treated in the ordinary manner by smelting.
- the sulphuric acid which would otherwise be formed is destroyed by the action of the hydrocarbon flame and the air which is admitted for this purpose above the burning ore.
- the combustion of the sulphur takes the place of a considerable portion of fuel and furnishes and waste fine coal, may be used.
- Figure l is a central ver tical section on a: as of Fig. 2.
- Fig. 2 is a plan view of the furnace.
- A represents the walls of the furnace.
- B is the hearth, having numerous perforations 1). Beneath the hearth is an air-supply pipe 0, through which air under pressure is introduced.
- F is the outlet, connected with any suitable cooling or collecting apparatus.
- e e are openings for charging in the ore, and e e are covers for the same.
- the object is to drive off a certain proportion of the sulphur, zinc, and lead, but not to melt the ore.
- the aim is to form a clinker orscoria. If the ore were melted, it would be fatal to the working of the process. Itis not in any sense a desulphurizing process, as it aims to retain quite a large percentage of the sulphurin the clinker, this also being an essential part of the process.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
(Specimens I. L. BARTLETT. rnocnss 01? TREATING SILVER AND ZING 0113s. No. 420,030.
Patented Jan. ,28, 1890.
PETERS, Fhnla-Uthcgrapl'vln Washinglum u c UNITED STATES ATENT FrIcE.
FRANK L. BARTLETT, OF PORTLAND, MAINE.
PROCESS OF TREATING SILVER AND ZINC ORES.
SPECIFICATION forming part of Letters Patent No. 420,030, dated January 28, 1890.
Application filed July 20, 1889- Serial No. 318,100. (Specimens) To all whom it may concern:
Be it known that I, FRANK L. BARTLETT, a citizen of the United States, residing at Portland, in the county of Cumberland and State of Maine, have invented certain new and useful Improvements in the Process of Treating Silver and Zinc Ores; and I do declare the following to be a'full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same, reference being had to the accompanying drawings, and to the letters of reference marked thereon, which form a part of this specification.
This invention relates to the treatment of the so-called sulphuret ores, more particularly such ores as contain large quantities of zinc in the form of zinc sulphuret, together with more or less silver, lead, copper, dzc.
According to the methods hitherto in common use these ores have been carefully roasted to expel the sulphur and then smelted with an excess of some other ore containmg no zinc. When the zinc was volatilized under these conditions without the presence of sulphur, it carried off with it large quantities of silver, which was not only lost, but if pigment was made greatly injured the quality of it. A further diificulty was occasioned by the action of the zinc on the slag, which was made thick and pasty by its presence, making it difficult to separate out the precious metals, and thus causing further losses. WVhen the ore was treated in a raw or unroasted state large quantities of sulphuric acid, which is very destructive, were given off.
Many attempts have been made to expel the zinc without undue loss of silver, but, so far as I am aware, without success, for th reasons above stated.
The object of the present invention is to devise a method of treatment whereby the zinc may be carried off in the form of fume without taking with it any appreciable amount of silver, and the silver left behind in the slag to be again smelted by the usual methods.
The invention is based on the factbelieved to be hitherto unknown that when ores containing silver and zinc are burned in the presence of an excess of sulphur the zinc escapes withouttaking with it any of the silver.
The process consist-s, broadly, of mixingthe ore with ahydrocarbon fuel, adding an excess of sulphur in some suitable form if the ore does not contain an excess of sulphur, burning it in the presence of an air-blast forced uniformly through the mass from the under side thereof, and admitting air above the burning ore to destroy the sulphuric acid which would otherwise be given 05.
By an excess of sulphuris meantaquantity equal to or exceeding the amount of the zinc content.
A fair example of the ores which it is designed to treatby this process would contain zinc, thirty per cent; lead, ten per cent; iron, ten per cent; sulphur, twenty per cent.; silica, thirty per cent. To this should be added sulphur enough to equal the amount of zinc contained in the oreas, for instance, fifty parts of iron and copper sulphide. If the ore contained sulphur equal to or greater in amount than the zinc, no sulphur would be added.
In carrying out the process I prefer to proceed as follows, viz: I take the raw ore and then crush it to a pea and grain size, and mix it with two-thirds,by weight, of finely-divided petroleum oils or residues, bituminous coal, saw-dust, or other flaming fuel. I then charge it into a furnace having a perforated hearth, in a shallow layer about four inches deep.
The Wetherel hearth, so called, with some modifications, is well suited to my process. The ore is burned in presence of an airblast, which is forced up through the perfo rated hearth, and a sufficient quantity of air.
is also forced in through openings in the sides of the furnace above the layer of ore. The zinc and lead, it any are present, are largely given oif in the form of fume, and may be collected in a bag-room or by other suitable means. Part of the sulphur unites with the copper, iron, silver, and gold, and forms a cinder or scoria, which retains all the non-volatile metals,wh ich may be subsequently treated in the ordinary manner by smelting. The sulphuric acid which would otherwise be formed is destroyed by the action of the hydrocarbon flame and the air which is admitted for this purpose above the burning ore. The combustion of the sulphur takes the place of a considerable portion of fuel and furnishes and waste fine coal, may be used.
In the accompanying drawings I illustrate a furnace suitable for carrying my process into effect.
In the drawings, Figure l is a central ver tical section on a: as of Fig. 2. Fig. 2 is a plan view of the furnace.
A represents the walls of the furnace.
B is the hearth, having numerous perforations 1). Beneath the hearth is an air-supply pipe 0, through which air under pressure is introduced.
F is the outlet, connected with any suitable cooling or collecting apparatus.
e e are openings for charging in the ore, and e e are covers for the same.
(I dare a set of air-supply pipes passing through the walls of the furnace and entering the combustion-chamber at a comparatively small distance above the hearth. These pipes are supplied with air from the pipe D. The ore and fuel are charged in through the openings e e, forming a shallow layer on the hearth or bottom B. Airis forced up through the perforated bottom 13 and through the layer of ore. Air is also blown in or allowed to enter through the pipes (Z d, for the purpose already pointed out.
It should be stated that unless a fuel is used containing much hydrocarbon sulphuric acid will be formed. Coke and anthracite coals alone cannot be used, since the necessary reaction upon the sulphur fumes will not take placeexcept in the presence of a hydrocarbon flame.
I am aware that hydrocarbon fuel has been mixed with ores containing sulphur and burned by means of an air-blast forced through the mass for the purpose of expelling the sulphur; but, so far as I am aware, low-grade zinc ores have not been treated by burning them with hydrocarbon fuel and a quantity of sulphur equal to or greater than the amount of zinc in the ore for producing a zinc pigment and retaining the silver. The process therein described is particularly adapted to be used with high-grade ores containingfromtwentyfive to fifty per cent. of zinc. The zinc is not entirely expelled; but the zinc content is reduced, so that it may be treated by the scoritying process set forth in my patent, No. 406,870, dated July 16, 188$),which is adapted to remove all the zinc from ores containing an amount less than twenty-five per cent.
In the present process the object is to drive off a certain proportion of the sulphur, zinc, and lead, but not to melt the ore. In fact, the aim is to form a clinker orscoria. If the ore were melted, it would be fatal to the working of the process. Itis not in any sense a desulphurizing process, as it aims to retain quite a large percentage of the sulphurin the clinker, this also being an essential part of the process.
I claim- The herein-described process of treating ores containing zinc andsilver,which consists in mixing the ore with hydrocarbon fuel,s upplying sufficient sulphur to produce an excess of the same, burning in the presence of an air-blast forced uniformly up through the whole mass of ore, and supplying air to unite with the products of combustion above said mass, substantially as shown.
In testimony whereof I affix my signature in presence of two witnesses.
FRANK L. BARTLETT.
Witnesses:
S. W. BATES, WM. M. HAGGETT.
Publications (1)
Publication Number | Publication Date |
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US420030A true US420030A (en) | 1890-01-28 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US420030D Expired - Lifetime US420030A (en) | Process of treating silver and zinc ores |
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US (1) | US420030A (en) |
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- US US420030D patent/US420030A/en not_active Expired - Lifetime
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