US59693A - Improved process of treating sulphurous ores of copper - Google Patents
Improved process of treating sulphurous ores of copper Download PDFInfo
- Publication number
- US59693A US59693A US59693DA US59693A US 59693 A US59693 A US 59693A US 59693D A US59693D A US 59693DA US 59693 A US59693 A US 59693A
- Authority
- US
- United States
- Prior art keywords
- copper
- iron
- oxide
- lime
- treating
- 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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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title description 29
- 229910052802 copper Inorganic materials 0.000 title description 29
- 239000010949 copper Substances 0.000 title description 29
- 238000000034 method Methods 0.000 title description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 29
- 229910052742 iron Inorganic materials 0.000 description 15
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 13
- 235000011941 Tilia x europaea Nutrition 0.000 description 13
- 239000004571 lime Substances 0.000 description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical class Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 10
- 235000002639 sodium chloride Nutrition 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- UCNNJGDEJXIUCC-UHFFFAOYSA-L hydroxy(oxo)iron;iron Chemical compound [Fe].O[Fe]=O.O[Fe]=O UCNNJGDEJXIUCC-UHFFFAOYSA-L 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 235000011167 hydrochloric acid Nutrition 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 229910021653 sulphate ion Inorganic materials 0.000 description 5
- 235000011149 sulphuric acid Nutrition 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 235000013980 iron oxide Nutrition 0.000 description 4
- 239000001117 sulphuric acid Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 2
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241001248539 Eurema lisa Species 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910001296 Malleable iron Inorganic materials 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- JEWHCPOELGJVCB-UHFFFAOYSA-N aluminum;calcium;oxido-[oxido(oxo)silyl]oxy-oxosilane;potassium;sodium;tridecahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.O.O.O.[Na].[Al].[K].[Ca].[O-][Si](=O)O[Si]([O-])=O JEWHCPOELGJVCB-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- -1 for instance Chemical compound 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052595 hematite Inorganic materials 0.000 description 1
- 239000011019 hematite Substances 0.000 description 1
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229910001743 phillipsite Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000008707 rearrangement Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000009736 wetting Methods 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
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0054—Slag, slime, speiss, or dross treating
Definitions
- Puloerizatioa-Vc pulverize the ore so finely that it will pass through a sieve of one hundred threads to the inch, or thereabout, by means of the machinery already patented by us.
- the reaction is to change the magnetic oxide to 'colcothar and the oxide of copper to sulphate, which can at once he lixiviated, leaving the colcothar a soluble commodity.
- the heat is to be slightly raised toward the last of the treatment.
- Sulphuric acid may be replaced by hydrochloric, or the sulphate by a chloride (common salt, for instance, or chloride of iron or lime) in this manipulation.
- a chloride common salt, for instance, or chloride of iron or lime
- the proportion of acid or salt to be introduced will be indicated by the amount of oxide of copper present in the pulp, and the chemical equivalents of the salts desired to be formed with or from the oxide of copper must be supplied in the acid or salt intro-' quizd.
- ment or may be reduced to revived or sponge iron for use in the further operations of the process, as described under manipulation sixth, or maybe rendered malleable by manipulation seventh.
- the oxide is reduced by diffusion of gases, first, to a lower state of a oxidation, and, lastly, to metallic iron in spongy forms.
- the water of the wetting-wheel In order to accomplish the absorption of the acid gas by the water, the water of the wetting-wheel must be derived from the water-bottom of the furnace, and during the burning of ores the wetting-wheel must work a chlorodized spray, partly derived from the water-bottom and partly from the settling-tubs of the chemicalwheel, as will be hereinafter described.
- the general effect of the sulphurous acid evolved during the burning of the ores is to throw down insoluble sulphates of lime and substitute in solution chloride of copper in the water-bottom and tubs of the wetting-wheel.
- the freed chlorine not taken up by'the oxide of copper will always be in the form of hydrochloric acid, and will pass to the chemicalwheel, where it is taken up by milk of lime, and the chloride of lime returned to the wetting-wheel.
- the waterbottom, settling-tank, and tubs of the wettingwheel will contain in the pulp sulphate of lime, undissolved oxide of copper, magnetic oxide of iron, some unburned sulphide, perhaps, and residuary earths.
- the hydrated oxide of copper is reduced and refined in the ordinary Welsh way.
- the final products of the working are metallic copper, oxides of iron, and sulphur salts of lime.
- a muffle-furnace may be conveniently substituted for the reverberatory.
Landscapes
- 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
UNITED STATES PATENT ()FFIGE.
J. D. WHELPLEY AND J. J. STOREB, OF BOSTON, MASSACHUSETTS.
IMPROVED PROCESS OF TREATING SULPHUROUS ORES OF COPPER.
Specification forming part of Letters Patent No. 59,693, dated November 13, 1866.
To all whom it may concern Be it known that we, JAMES D. WHELPLEY and J A0013 J. STORER, of Boston, in the county of Suffolk ant State of Massachusetts, have invented a new and useful Method of Treating the Sulphurous Ores of Copper and iron oxides obtained from them 5 and I do hereby declare that the following is a full, clear, and exact description of the construction and operation of the same.
Our method of working the sulphurous ores of copper is as follows:
l. Puloerizatioa-Vc pulverize the ore so finely that it will pass through a sieve of one hundred threads to the inch, or thereabout, by means of the machinery already patented by us.
2. Aerial combustion and immediate Zinieia-- tion.We next burn the ore floated on an airblast in a heated flue, and lixiviate it in hot acidulated water, as described in previous patents and applications.
3. Burning without special fuel.After the flue has been heated in the earlier part of the burning we abandon the feeding of fuel to the water-furnace, and find that the radiation of heat from the Walls of the flue is sufficient to inflame the sulphuret, and the generation of heat by the combustion of the sulphur is sufficient to maintainthe heat of the flue. To this end we employ ores containing a large percentage of sulphur, or so mingled that a large proportion of sulphur is present.
4. Treatment of the oooides.--If the burning be slowly conducted the ore will be converted into soluble sulphate of copper and magnetic oxide of iron; but it may happen that, by rapid burning at a high degree of heat, the larger part of the copper will appear as difficultly-soluble oxide. hen this is the case we take the pulp of the tank, consisting of magnetic oxide, gangue, and difticultly-soluble oxide of copper, all in a finely-divided state,
' and intimately mingle with it sulphate of iron,
or wet it with sulphuric acid, and expose it at r a low red heat upon the floor of a reverberatory furnace, frequently stirring the mass. The reaction is to change the magnetic oxide to 'colcothar and the oxide of copper to sulphate, which can at once he lixiviated, leaving the colcothar a soluble commodity. The heat is to be slightly raised toward the last of the treatment.
Sulphuric acid may be replaced by hydrochloric, or the sulphate by a chloride (common salt, for instance, or chloride of iron or lime) in this manipulation. In either case We get a soluble salt of copper and insoluble coleothar.
The wetting of magnetic oxide with an acid to change it to eolcothar and subsequent treatment, as described, are new in the arts, and we consider this use of sulphuric and hydrochloric acids as a means of hyperoxidation to be valuable, and to point out a way by which we can obtain in mineral paints still brighter tints than we have at present.
The proportion of acid or salt to be introduced will be indicated by the amount of oxide of copper present in the pulp, and the chemical equivalents of the salts desired to be formed with or from the oxide of copper must be supplied in the acid or salt intro-' duced.
5. Limioiation and use of the centrifugal ma ehine.-\Ve now lixiviate the pulp obtained from the fourth manipulation, either in the ordinary way, or we place it in a centrifugal machine, such as is used in sugar-houses, but lined with felt of a loose texture, and direct a stream of pure water or water acidulated with sulphuric or hydrochloric acid, according to the nature of the salt formed in the fourth manipulation, into the center of the machine while in motion, dissolve out the soluble salt and oxide of copper, and render the iron oxide nearly pure. This may be smelted for iron, as hematite or magnetic oxide is usually smelted, may be ground in oil for a cheap pig-,
ment, or may be reduced to revived or sponge iron for use in the further operations of the process, as described under manipulation sixth, or maybe rendered malleable by manipulation seventh.
6. Manufacture of revived iron and cementation'.The magnetic oxide or the colcothar is now mingled with or placed adjacent to an equivalent amount of carbonaceous matter under a muffle or cover and heated to a red heat without access of air-current. A con venient way of doing this is to place two piles, one of iron oxide, the other of charcoal, on the floor ofa mutfle, adjacent to each other. Another mode would be to fill a porous crucible with oxide, place it in a larger crucible, pack the interval with coal-dust, and then lute a cover over the whole. In the latter case the heat must be nearly white. After a short time the oxide is reduced by diffusion of gases, first, to a lower state of a oxidation, and, lastly, to metallic iron in spongy forms. This we call revived iron. It is thrown into the disturber of the precipitating-tub, as described in a former application, and is in the bestform for precipitating cement copper from the solution obtained in the second and fifth manipulations.
7. Refining 0f sponge-iron after it has been revived-When the quantity of revived iron produced in the last manipulation is greater than needed in the precipitation of copper from its solution, we raise the sponge to a welding-heat without access of air, and, passing it through roughing rolls or squeezers, produce a fine quality of malleable iron. A suitable muffle for this purpose is the ordinary glass pot with flat bottom and domed top.
Variations in second, third, fourth, and fifth manipulations are as follows:
In case we have an ore carrying but little sulphur, like the lean Canadian ores, Phillipsite, or ores partly pyritous and partly oxidized, we shall be obliged to employ chlorine as a solvent, and this introduces some modifications in the burnings and subsequent treat,
ment.
We prepare in the water-bottom of our furnace a bath of chloride of lime and hydrochloric acid, either by admitting into the tower through one of the inspection-holes a pipe communicating with a retort containing common salt and sulphuric acid, or by pouring hydrochloric acid into the water of the trough,- and saturatin g with carbonate of lime until two-thirds of the hydrochloric acid is salified. In order to accomplish the absorption of the acid gas by the water, the water of the wetting-wheel must be derived from the water-bottom of the furnace, and during the burning of ores the wetting-wheel must work a chlorodized spray, partly derived from the water-bottom and partly from the settling-tubs of the chemicalwheel, as will be hereinafter described.
The general effect of the sulphurous acid evolved during the burning of the ores is to throw down insoluble sulphates of lime and substitute in solution chloride of copper in the water-bottom and tubs of the wetting-wheel. The freed chlorine not taken up by'the oxide of copper will always be in the form of hydrochloric acid, and will pass to the chemicalwheel, where it is taken up by milk of lime, and the chloride of lime returned to the wetting-wheel.
The waterbottom, settling-tank, and tubs of the wettingwheel will contain in the pulp sulphate of lime, undissolved oxide of copper, magnetic oxide of iron, some unburned sulphide, perhaps, and residuary earths. The
solution will hold chlorides of iron, copper, and lime, from which the copper can be precipitated, as we have already described in a former part of this paper.
We now spread the pulp on the floor of a reverberatory furnace, and apply a gentle heat, never rising above the low red. The effect is, first, the evaporation of the water; the residuary sulphides are next chlorodized, and next the oxides of copper are converted into chlorides, while the chlorides of iron are converted into oxides, and the escaping chlorine, if any, is transmitted to the water-furnace, to be again employed. The mass in the reverberatory furnace now consists of red and black oxide of iron, insoluble salt of lime,
soluble chloride of copper, and residuary earths, the whole permeated by a fine sponge of soluble anhydrous chloride of lime. This we thoroughly pulverize and lixiviate with water, or, if necessary to extract all the copper, with dilute hydrochloric acid, and treat the lixiviate with milk of lime, which throws down hydrated oxide of copper, leaving chloride of lime in solution, to be used in the trough of the water-furnace or in lixiviating. If
there be lime in the mineral it can be turned to account by employing the crushed ore to precipitate the solution of chloride. The carbonate of copper would be treated similarly to the hydrated oxide.
The hydrated oxide of copper is reduced and refined in the ordinary Welsh way. The final products of the working are metallic copper, oxides of iron, and sulphur salts of lime. a
If carefully managed, but one burning in the reverberatory furnace will be required; but if a second is needed the pulp must be first wetted with. some of the acid waters of lixiviation containing chloride of lime.
In the operations subsequent to the treatment in the water-furnace a muffle-furnace may be conveniently substituted for the reverberatory.
We claim as our invention, and desire to secure by Letters Patent I 1. The seven manipulations above set forth in their order and with the variations described, as a process for treating sulphurets of copper.
2. The first, second, third, and sixth manipulations and the variations described, as a process for treatingsulphurous ores of copper.
3. The first six manipulations and the variations described, as a process for treating copper sulphurets.
4. The first, second, third, fifth, and sixth manipulations and the variations thereof caused by omitting the third and sixth and employing the method described after seventh, as a process for treating copper sulphurets.
5. The rearrangement of the equivalents of the ore by the heat generated by its own combustion in presence of oxygen and without I diffusion of gases between carbon and the oxother fuel than that contained in itself, subides at a low degree of heat and without ourstantially as described. rents of air, substantially as described.
6. The employment for the lixiviation of minerals of the centrifugal drying-machine, as described, and the arrangement of the felt lining upon its interior, substantially as de- Witnesses: scribed. Tnos. WM. CLARKE,
7. The revival of iron from iron oxides by CHAS. J. BATEMAN.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US59693A true US59693A (en) | 1866-11-13 |
Family
ID=2129232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US59693D Expired - Lifetime US59693A (en) | Improved process of treating sulphurous ores of copper |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US59693A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4003740A (en) * | 1976-01-06 | 1977-01-18 | Allied Chemical Corporation | Recovery of copper from copper sulfide ores containing copper and iron |
-
0
- US US59693D patent/US59693A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4003740A (en) * | 1976-01-06 | 1977-01-18 | Allied Chemical Corporation | Recovery of copper from copper sulfide ores containing copper and iron |
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