US7670A - Bichakd s - Google Patents
Bichakd s Download PDFInfo
- Publication number
- US7670A US7670A US7670DA US7670A US 7670 A US7670 A US 7670A US 7670D A US7670D A US 7670DA US 7670 A US7670 A US 7670A
- Authority
- US
- United States
- Prior art keywords
- silver
- gold
- gold bullion
- bullion
- acid
- 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
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 27
- 229910052737 gold Inorganic materials 0.000 description 27
- 239000010931 gold Substances 0.000 description 27
- 239000004332 silver Substances 0.000 description 16
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 15
- 229910052709 silver Inorganic materials 0.000 description 15
- 238000000034 method Methods 0.000 description 14
- 239000002253 acid Substances 0.000 description 11
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 235000011149 sulphuric acid Nutrition 0.000 description 8
- 239000001117 sulphuric acid Substances 0.000 description 8
- 150000007513 acids Chemical class 0.000 description 7
- 239000012535 impurity Substances 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 238000007670 refining Methods 0.000 description 7
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 5
- 229910045601 alloy Inorganic materials 0.000 description 5
- 239000000956 alloy Substances 0.000 description 5
- 229910052725 zinc Inorganic materials 0.000 description 5
- 239000011701 zinc Substances 0.000 description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 230000006872 improvement Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229940074355 nitric acid Drugs 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- 229910001316 Ag alloy Inorganic materials 0.000 description 1
- 229910001020 Au alloy Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010011971 Decreased interest Diseases 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052571 earthenware Inorganic materials 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000000266 injurious effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003378 silver Chemical class 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 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
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
Definitions
- the improvement and advantages in the art of refining gold attained by my invention and discovery are, first, the comparatively easy separation from gold bullion of theimpurities with which it is in combination without using silver for quartation, without waste of silver, and without costly apparatus; second, much greater economy of time,labor, and expense; third,the saving ot'interest; fonrt-h,the use of lower temperatures than in the usual methods, and vessels of lead not subject to fracture; fifth, the rendering of the work of the refiner more simple, expeditious, and free from'the necessity of his constant attention, also less injurious to his health, and no longer a. nuisance it conducted in densely-populated places.
- my invention and discovery consists in bringing gold bullion containing silver or other impurities into a loose, divided, pulverulent, or spongy state, texture, or disintegrated molecular condition, so that all impurities it may contain can readily be removed by acids.
- the gold bullion to be refined may be of any quality.
- My first or preparatory operation is to make an adulterated alloy or mixture by melting and mechanically stirring the gold bullion with a sufficient quantity of zinc, usually two or three times the weight of the gold bullion to be refined, and after the melted alloy has been well stirred it is granulated by pouring it into water, according to the usual methods.
- the granulated alloy is treated, in wooden vats lined with lead, with dilute sulphuric acid, which removes the zinc employed for adulteration and leaves impure or argentiferous gold in a finely-divided pulverulent or spongy state or in a disintegrated molecular condition.
- the hydrogen which escapes during this operation should be conducted by wooden or other pipes into the open air.
- heat is not used or required, and but little more acid is employed than will form sulphate of zinc with that metal used for adulteration; or, in other words, the
- copper, 8cc.- -to render the alloy base enough for the action of acid, as used in the second operation secondly, that, in reference to the second operation above described, it. may be varied by using muriatic, nitric, or other acid instead of dilute sulphuric acid; thirdly, that as the processes, first, of alloying and granulating, and, secondly, of treating the alloyed gold bullion with acids, are intended, as above.
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
' lain, or earthenware.
these methods are, first, the withdrawing of Brennan s. MGGULLOH, or PRINCETON, new JERSEY.
PROCESS OF REDUCING GOLD BULLION.
Specification forming part oi Letters Patent No. 7,6'20, dated September 24, 1850.
To all whom it may concern:
Beit known that I, Brennan S. McOULLon, late of the city of Philadelphia, and now residing in Princeton, New Jersey, have invented and discovered a new, useful, and important Method of Separating'silver and other Impurities from Gold Bullion, the same being an improvement in the art ofrefining gold for coinage and other purposes, of which the following is a, specification.
For the full and exact understanding of my discovery I will describe so much of the meth ods heretofore known and now usually practiced as is necessary. They consist, in part, of the operation of quartation, as it' is calledthat is,'of melting and intimately combining with the gold bullion to be refined two to three timesitsweightof silver. Toextractthissilver, together with that and all impurities originallycontained in the gold bullion itself, from the mixed alloy of gold and silver then requires .that it be granulated by pouring it, while melted, into water, and subsequently that it be digested, either in sulphuric acid concentrated to 66. Baum at the high temperature of the ebullition thereof and in costly platinum vessels, or in nitric acid of 36 Baum at temperatures not lower than 212 Fahrenheit, or the boiling-point of water, and in fragile vessels of glass, porce- The chief objections to large quantities of silver from use as circulating capital; second, the great labor, expense, and delay attending the successive granulation,separation,and recovery from solution of that silver; third, the loss of interest; fourth, the wastage of silver; fifth, the very high cost and expensive repairs ofthe large platinum retorts required in the sulphuric-acid process, and the frequent breaking of the vessels used in the nitric-acid process, attended with more or less loss of the precious contents thereof.
The improvement and advantages in the art of refining gold attained by my invention and discovery are, first, the comparatively easy separation from gold bullion of theimpurities with which it is in combination without using silver for quartation, without waste of silver, and without costly apparatus; second, much greater economy of time,labor, and expense; third,the saving ot'interest; fonrt-h,the use of lower temperatures than in the usual methods, and vessels of lead not subject to fracture; fifth, the rendering of the work of the refiner more simple, expeditious, and free from'the necessity of his constant attention, also less injurious to his health, and no longer a. nuisance it conducted in densely-populated places.
The nature of my invention and discovery consists in bringing gold bullion containing silver or other impurities into a loose, divided, pulverulent, or spongy state, texture, or disintegrated molecular condition, so that all impurities it may contain can readily be removed by acids.
The obtaining of gold in such a state or reducingit from a compact to a disintegrated condition, that it may be attacked by acids, forms no part or object of the methods now in use, and it is this preliminary mechanical operation which gives to myimprovement in the art of refining gold the great advantage of dispensing with the useoflarge quantitiesofsilver, thus causing economy in labor, time, and expense.
To enable those skilled in the art of refining gold bullion to understand and use myinvention and discovery, I now describe its nature and operation, to wit:
First. The gold bullion to be refined may be of any quality. My first or preparatory operation is to make an adulterated alloy or mixture by melting and mechanically stirring the gold bullion with a sufficient quantity of zinc, usually two or three times the weight of the gold bullion to be refined, and after the melted alloy has been well stirred it is granulated by pouring it into water, according to the usual methods.
Secondly. The granulated alloy is treated, in wooden vats lined with lead, with dilute sulphuric acid, which removes the zinc employed for adulteration and leaves impure or argentiferous gold in a finely-divided pulverulent or spongy state or in a disintegrated molecular condition. The hydrogen which escapes during this operation should be conducted by wooden or other pipes into the open air. In this second operation heat is not used or required, and but little more acid is employed than will form sulphate of zinc with that metal used for adulteration; or, in other words, the
acid is used in nearly atomic proportions. The object sought by the two operations just described is only to operate on the gold bullion in such a manner as to reduce it to a disintegrated or spongy state, in which it shall no longer be capable of resisting or protecting the impurities it may contain from the reaction of acids, as it does when in compact form or consistence, which resistance or protection has been the chief obstacle with which the art of refining has heretofore had to contend.
Thirdly. When I have obtained the gold bullion in'a pulverulent or spongy state, incable of resisting the reaction of acids, by thus treating an alloy of it with dilute sulphuric acid all the silver which may have been originally combined with it is still retained by it,
dilute sulphuric acid being incapable of extracting' any portion thereof. To remove this silver I digest the disintegrated bullion, as in the methods now employed, either in nitric or sulphuric acid, with heat and in any suitable vessel, sulphate of zinc being first entirely removed by washing.
Finally. The operations are terminated by cupelling, the refined gold or ineltin g it with such fluxes as borax, niter, &c., and casting itinto ingots or bars. If the operations have been properly performed these ingots will be ductile and of a firmness varying from 98.5 to 95.5 per cent.,theresidual impurity being silver, an d from the solution thereof in nitric or sulphuric acid the silver extracted from the gold bullion is then to be recovered by the usual and wellknown ehemicalmethods now in use.
For the purpose of explaining the principle which characterizes my invention and discovcry, and the several modesin which I have contemplated its application in the art of refining gold bullion, I new state, first, in reference to my first operation above described, that it may be varied bymelting the gold bullion to be refined with a suficient quantity of some other metal or metals baser than silver-such as iron,
copper, 8cc.- -to render the alloy base enough for the action of acid, as used in the second operation secondly, that, in reference to the second operation above described, it. may be varied by using muriatic, nitric, or other acid instead of dilute sulphuric acid; thirdly, that as the processes, first, of alloying and granulating, and, secondly, of treating the alloyed gold bullion with acids, are intended, as above.
What I particularly claim as my'inventionand discovery, and desire to secure by Letters Patent as a new and useful improvement in the art of refining gold bullion, is-
1. The reduction of argentiferous and other gold bullion, as a preparatory process in the art of refining thereof, into a pulverulen't' or spongy state, or a disintegrated'molecular condition, by the means particularly of fusion therewith, and, the subsequent removal by acids therefrom, of zinc or other metal baser than silver which will produce the desiredefi'ect, for the purpose of then separating by acids from such gold bullion the silver and other impurities which it may contain, without quartation with silver or any intermediate process, in'order to fit the gold for coinage and other uses. 2. In addition to the above processes, the pulverizing, by grinding, crushing, or percussion, of gold bullion rendered brittle by union with lead, solder, or other like base metal, for
the purpose set forth in the specification.
RIUHD. S. MGUULLOH.
Witnesses:
-VVoons BAKER,
JAS. S. GREEN.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US7670A true US7670A (en) | 1850-09-24 |
Family
ID=2067980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US7670D Expired - Lifetime US7670A (en) | Bichakd s |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US7670A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857107A (en) * | 1985-09-12 | 1989-08-15 | Fine Metals Export Corporation Limited | Gold inquartation process |
-
0
- US US7670D patent/US7670A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857107A (en) * | 1985-09-12 | 1989-08-15 | Fine Metals Export Corporation Limited | Gold inquartation process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4188362A (en) | Process for the treatment of platinum group metals and gold | |
| CA2393511C (en) | Refining of metallurgical grade silicon | |
| US2396792A (en) | Refining nickel | |
| US7670A (en) | Bichakd s | |
| US2195433A (en) | Process for producing boron-copper alloys | |
| NO134876B (en) | ||
| JPH03199314A (en) | Decoppering method for iron scrap | |
| JPH04224639A (en) | Method for purification of lead wherein copper is especially removed | |
| RU2112064C1 (en) | Method of processing of products based on chalcogenides of base metals containing metals of platinum group and gold | |
| US2029898A (en) | Method of purifying magnesium | |
| BE1006723A3 (en) | Sludge treatment of high nickel content. | |
| US1957837A (en) | Method of purifying lead, tin, and lead-tin alloys | |
| US890160A (en) | Process of removing gold, silver, copper, and platinum from lead alloys. | |
| EP0043646B1 (en) | Separation of chromium from scrap | |
| US4173467A (en) | Process for recovering valuable metals from superalloy scrap | |
| RU2119541C1 (en) | Method and apparatus for recovering precious metals from intermediate products | |
| US2043575A (en) | Process for detinning lead alloys | |
| US20210071284A1 (en) | Method for hydrometallurgical processing of a noble metal-tin alloy | |
| USRE22270E (en) | Process fob the manufacture of | |
| US1841207A (en) | Treatment of ores, metallurgical products, residues, and the like, for the recovery of platinum metals | |
| JP3784331B2 (en) | Method for purifying gold-containing gallium and method for collecting gold from gallium containing gold | |
| US370338A (en) | Daeley c | |
| US12585A (en) | Improvement in processes for refining jewelers scraps | |
| US1845145A (en) | Process of making an alloy | |
| US509634A (en) | And cabell |