US1063568A - Process of precipitation of material from cyanid solutions. - Google Patents
Process of precipitation of material from cyanid solutions. Download PDFInfo
- Publication number
- US1063568A US1063568A US63873311A US1911638733A US1063568A US 1063568 A US1063568 A US 1063568A US 63873311 A US63873311 A US 63873311A US 1911638733 A US1911638733 A US 1911638733A US 1063568 A US1063568 A US 1063568A
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- United States
- Prior art keywords
- precipitant
- solutions
- precipitation
- metals
- zinc
- 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
- 238000000034 method Methods 0.000 title description 16
- 238000001556 precipitation Methods 0.000 title description 9
- 239000000463 material Substances 0.000 title description 4
- 229910052751 metal Inorganic materials 0.000 description 19
- 239000002184 metal Substances 0.000 description 19
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 16
- 150000002739 metals Chemical class 0.000 description 15
- 239000011701 zinc Substances 0.000 description 15
- 229910052725 zinc Inorganic materials 0.000 description 15
- 239000002244 precipitate Substances 0.000 description 13
- 229910045601 alloy Inorganic materials 0.000 description 10
- 239000000956 alloy Substances 0.000 description 10
- 230000001376 precipitating effect Effects 0.000 description 8
- 239000003517 fume Substances 0.000 description 5
- 239000010970 precious metal Substances 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 101001126084 Homo sapiens Piwi-like protein 2 Proteins 0.000 description 1
- 102100029365 Piwi-like protein 2 Human genes 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 101150115956 slc25a26 gene Proteins 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- C22B43/00—Obtaining mercury
Definitions
- F is a filter press, shownin this case with the discharge pipe D from the pump forming the feed inlet at the top and with opened, the tube mill revolved, the pump P is started and the solution allowed to enter the mill, whereupon it is subjected to the grinding action of the same. From the mill T, the solution is drawn through the pipe C to the pump P, thence forced through the pipe D to the filter press F,
- valves 0 and c I also do not limit myself to the precise form of grinding apparatus described above, nor to the precise arrangement of the plant nor the aggregation of component parts shown. But I employ any form of grinding apparatus, whether closed or open, and any arrangement or disposition of plant which may be found desirable according to conditions, or I may re-arrange or eliminate any desired parts from time'to time, and may substitute for the filter press any equivalent apparatus or any apparatus which will accomplish the mechanical separation of the valuable suspended material from the solution, either by filtration, settlement or other method of separation or concentration.
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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
G. W. MERRILL. mooass 0F PREOIPlTATION 0F MATERIAL FROM OYANID SOLUTIONS. APPLIOATION FILED JULY 15, 1911.
1,063,5 Patefited June 3,1913.
M M J t; 1"; flue M4211 6M4 6276C r UNITED STATES PATENT OFFICE.
CHARLES W. MERRILL, OF BERKELEY, CALIFORNIA.
PROCESS OF PRECIPITATION 0F MATERIAL FROM CYANID SOLUTIONS. I
Specification of Letters Patent.
I atented June 3, 1913.
Application filed July 15, 1911. Serial No. 638,733.
, cation.
In practice zinc threads or shavings if necessary and zinc fume or dust have heretofore been used in order to precipitate precious metals from cyanid solutions. The objections to the use of threads or shavings of zinc are first, the cost of preparing them, second, that even when tightly packed, a number of boxes must be placed in tandem in order to insure each particle of solution to be treated coming in contact with the zinc, which results in an unnecessarily large consumption of zinc and cyanid; third, the zinc becomes rapidly polarized and coated and must be moved and washed frequently to insure good precipitation; fourth, this frequent handling oflers opportunity for theft. Hence the use of zinc dust has overcome many of these objections, largely superseding the use of threads or shavings,
but it too has defects which have developed in its use, and some of which are as follows: First, it contains a widely varying proportion of oxid and other impurities, many of which are not only useless as precipitating media, but destructive of cyanid, or difficult to eliminate in the subsequent refining of the precipitate. Second, the increase in the use of the zinc fume in this art has resulted in an advance in the cost of this material until it now exceeds that of spelt-er. Third, the transportation and storage of the fume is attended with danger and abnormal expense on account of its inflammable and explosive nature.- Fourth, unless hermetically sealed, it oxidizes rapidly, particularly in hydrometallurgical plants where the atmosphere is humid, thus resulting in a serious deterioration of its precipitating efliciency. Furthermore, owing to its well-known prop- .erty of malleability, zinc itself is commi nuted with great difficulty by the friction of one zinc surface upon another, and attempts to so produce a pulverulent precipitate for cyanid solutions have not found successful use in the art.
Now, I have discovered that if cyanid solutions containing the precious metals be passed through a grinding-apparatus, one
at least of the grinding surfaces of which -1s composed of mm, aluminum, or other metal or alloy, which will precipitate the desired metals from their cyanid solutions, and preferably such alloys as are more brittle than metallic zinc, and the mixture of solution, precipitate and precipitant conducted to a collector or a filter, an economic, easily regulated and metallurgically efficient processresults, which is free from the defects enumerated in the zinc thread and zinc fume processes, and one in which the precipitant can be easily comminuted.
The method of conducting the process will be best understood by reference to the accompanying sheet of drawings forming a part of this specification, which shows one of many arrangements of plant, in which the process forming the subject of the present invention can be carried out; but the apparatus itself and the arrangement of the same form no part of the invention, and may be varied both in the arrangement and number ,of the parts and of the entire system from time to time, as may befound necessary, according to the conditions under which the process is applied in practice.
In the drawing, U is a receiver for the unprecipitated solution; B, an inletpipe, G is a discharge pipe, T is a revolving tube mill containing rollers or balls, composed wholly or in part of a precipitant, and preferably lined with the same material and driven from any convenient source of power.
C is a suction of a pump P, and D is a discharge pipe of the'samc.
U and C are inlet and outlet valves of the grinding apparatus.
F is a filter press, shownin this case with the discharge pipe D from the pump forming the feed inlet at the top and with opened, the tube mill revolved, the pump P is started and the solution allowed to enter the mill, whereupon it is subjected to the grinding action of the same. From the mill T, the solution is drawn through the pipe C to the pump P, thence forced through the pipe D to the filter press F,
and thence through the filter F, which not only retains the precipitate and precipitant, but which also effects are precipitation of more of the metallic contents of the solution and permits the solution to pass into the launder L and thence to the receiver E.
I prefer to use a suitable alloy for a grinding surface because of the increased precipitating efficiency caused by the galvanic couple, and I also prefer to use an alloy more brittle than zinc because of the greater ease with which such an alloy may be comminuted, a tube mill for the grinding apparatus containing rollers or balls of said alloy; and I also prefer to conduct the precipitation without such retardation as will permit of the settlement of the pulve'rulent precipitant and without exposure of the precipitant and precipitate to the influence of oxidation, from the grinding apparatus to the filter or collector, but I do not limit myself to these special features.
In the practical operation of the process it may be desirable to'so adjust the flow of the solution through the grinding apparatus as to attain a proper proportion between the comminuted precipitant and the amount of solution, and this may, of course, be accomplished .by the valves 0 and c I also do not limit myself to the precise form of grinding apparatus described above, nor to the precise arrangement of the plant nor the aggregation of component parts shown. But I employ any form of grinding apparatus, whether closed or open, and any arrangement or disposition of plant which may be found desirable according to conditions, or I may re-arrange or eliminate any desired parts from time'to time, and may substitute for the filter press any equivalent apparatus or any apparatus which will accomplish the mechanical separation of the valuable suspended material from the solution, either by filtration, settlement or other method of separation or concentration.
In cases where the attritive action is insuflicient to liberate an adequate amount of precipitant, or where it is desired to reinforce the precipitation by an increased amount of precipitant, I may add an additional amount of precipitant or alloy, such as zinc fumes, zinc shavings, or an alloy in the form of granules, either to the collecting tank, to the grinding apparatus, to the filter, or to the solution, wherever convenient between its discharge from the container, where the precious metals are dissolved from the ore and the discharge of the solution from the apparatus in which the precipitate and precipitant are collected, the result of which is to form a precipitate and a precipitant which would pass into the grinding apparatus and thus partially precipitate the solution before it comes in contact with the precipitant incorporated in the grinding surface of the comminuting apparatus.
I claim as my invention:
1. The hereinbefore described process of precipitation of metals from their solutions, which consists in causing the said solutions to pass througha comminuting apparatus, in which they are brought in contact with a metallic precipitant of said metals, with which has been incorporated a substance capable of intensifying the comminution of said precipitant.
2. The hereinbefore described process of precipitation of metals from their solutions,
which consists in causing the said solutions to pass through a comminuting apparatus in which they are brought in contact with a metallic precipitant of said metals, with which has been incorporated a metallic sub-' stance capable of intensifying the comminution of said precipitant.
3. The hereinbefore described process of precipitation of metals from their solutions, which consists in causing said solutions to pass through a comminuting apparatus in which they are brought in contact with a brittle alloy containing a metallic precipitant of said metals.
4. The hereinbefore described process of precipitating metals from cyanid solutions, which consists in passing the solution, which has already been partially precipitated, together with such a partial precipitate and precipitant through a comminuting apparatus.
5. The hereinbefore described process of precipitating metals from cyanid solutions, which consists in passing the solution, which has already been partially precipitated, together with such a partial precipitate and precipitant, through a comminuting apparatus in which they come in contact with a precipitant.
6. The hereinbefore described process of precipitating metals from cyanid solutions, which consists in passing a solution which has already been partially precipitated, together with such partial precipitate and precipitant, through a revolving tube mill, in which they are brought in contact with a brittle alloy containing a metallic precipitant of said metals.
7. The hereinbefore described process of precipitating metals from cyanid solutions, which consists in passing the said solutions which have already been partially precipitated. together with such partial precipitate and precipitant through a revolving tube mill in which they are brought in contact with a metallic precipitant of said metal, alloyed with a metal capable of producin a galvanic couple favorable to the precipitation of the desired metals from their solutions.
8. The hereinbefore described process of precipitating metals from cyanid solutions,
which consists in passi a solution which In testimony, that I claim the foregoing 10 has already been partial y precipitated, toas my invention, I have signed my name in gether with such partial recipitate and prepresence of two witnesses, this thirtieth day cigitililntilthroughba refioving tube milli1 in of June, 1911.
5 w ic t ey are rou t in contact wit a precipitant alloyed with a metal capable of CHARLES MERRILL producing a galvanic couple, favorable to Witnesses: the precipitatlon of the desired metals from LOUIS D. MILIs, their solutions. C. C. BROADWATER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US63873311A US1063568A (en) | 1911-07-15 | 1911-07-15 | Process of precipitation of material from cyanid solutions. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US63873311A US1063568A (en) | 1911-07-15 | 1911-07-15 | Process of precipitation of material from cyanid solutions. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1063568A true US1063568A (en) | 1913-06-03 |
Family
ID=3131814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US63873311A Expired - Lifetime US1063568A (en) | 1911-07-15 | 1911-07-15 | Process of precipitation of material from cyanid solutions. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1063568A (en) |
-
1911
- 1911-07-15 US US63873311A patent/US1063568A/en not_active Expired - Lifetime
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