US569334A - Process of extracting gold - Google Patents

Process of extracting gold Download PDF

Info

Publication number
US569334A
US569334A US569334DA US569334A US 569334 A US569334 A US 569334A US 569334D A US569334D A US 569334DA US 569334 A US569334 A US 569334A
Authority
US
United States
Prior art keywords
bromin
chlorid
chlorin
gold
ore
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
Application number
Publication date
Application granted granted Critical
Publication of US569334A publication Critical patent/US569334A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44Treatment or purification of solutions, e.g. obtained by leaching by chemical processes

Definitions

  • This invention relates to an improved process of extracting gold from ores in an economical and simple manner.
  • chlorin readily combines with the bases in the ore and dissolves the gold, but as chlorin is a gas it cannot be employed in its gaseous form without pressure, which renders its use both complicated and expensive.
  • a liquid carrier viz., bromin, with which it forms bromin chlorid, (BrOl,) which is a volatile liquid that contains the chlorin in a liquid form.
  • the chlorin constituent of this liquid has the property of very readily combining with the bases of the ores, for which the chlorin has the greater and the bromin the lesser affinity.
  • bromin is by far the more expensive constituent of the bromin chlorid, and therefore the employment of the latter would be commercially impracticable if means were not provided for recovering the bromin.
  • I provide such means and recombine the bromin of the decomposed bromin chlorid with a fresh body of chlorin, so as to again form bromin chlorid.
  • This bromin chlorid may be used upon a new supply of ore and in this way the process is practically continuous and very inexpensive, so that it is well adapted for commercial purposes.
  • the pulverized ore is placed into a revolving barrel or cylinder a, and upon it is poured a solution in water of bromin chlorid, which may be prepared by any of the well-known methods.
  • bromin chlorid which may be prepared by any of the well-known methods. The amount of bromin chlorid necessary to completely dissolve the gold va- Serial No. 569,035. (No specimens.)
  • the mixture is stirred by the rotation of the barrel a for from one to three hours, when the gold will be dissolved.
  • the dissolved gold is leached and separated from the gangue by any suitable method, and is collected in a tank h.
  • the solution in this tank will contain the gold as well as other soluble bases which may have been present in the ore.
  • I may set free the old chlorin from its combinations with the bases of the ores by the introduction of an oxidizing agent.
  • the liquid in the tank h is heated in any desired manner, preferably by conducting into it a current of steam, which is drawn from a suitable generator d.
  • the steam will separate the bromin chlorid from the solution in the form of vapor, which is carried by the escaping steam through a pipe e and into the condenser f.
  • bromin chlorid is avery volatile IOO liquid
  • its complete separation from the solution in the tank l) by the aid of heat, may be readily effected.
  • the condenser f which serves to liquidize the bromin-chlorid vapors, may be of an suitable construction, the drawing showing a Gay-Lussac tower, into which Water is admitted Yfrom pipeg.
  • the liquidized brornin chlo rid collects in a tank h, having a vent c', that dips into a tank j, containing an alkali, to absorb any of the vapors that .may escape.
  • the bromin chlorid is in condition to be used over again upon a fresh body of ore.

Description

(No Model.)
B. G. HINMAN. PRocess 0F EXTRAGTING GOLD.
Patented Oct. 13, 1896..
flare/ahr.-
we nofws PETERS co, Pnoraumo., wAsHmcrcN. n. c.
Nrrrnn STATES BERTRAND O. HINMAN, OF YORK, N. Y., ASSIGNOR TO THE lGOLD AND BROMINE SEPARATING COMPANY, OF SAME PLACE AND IVEST VIRGINIA.
PROCESS OF EXTRACTING GOLD.
SPECIFICATION forming part of Letters Patent No. 569,334, dated October 13, 1896.
Application filed November 15, 1895.
To all whom, t may concern-.-
Be it known that I, BERTRAND C. HINMAN, a citizen of the United States, and a resident of New York, in the county of New York and State of New York, have invented cert-ain new and useful Improvements in Processes of Extracting Gold, of which the following is a specification.
This invention relates to an improved process of extracting gold from ores in an economical and simple manner.
It is well known that chlorin readily combines with the bases in the ore and dissolves the gold, but as chlorin is a gas it cannot be employed in its gaseous form without pressure, which renders its use both complicated and expensive. I propose to combine the chlorin with a liquid carrier-viz., bromin, with which it forms bromin chlorid, (BrOl,) which is a volatile liquid that contains the chlorin in a liquid form. The chlorin constituent of this liquid has the property of very readily combining with the bases of the ores, for which the chlorin has the greater and the bromin the lesser affinity. Thus not only do I obtain the beneficial effect of both these halogens but the chlorin in its liquid form is more readily handled.
Of course the bromin is by far the more expensive constituent of the bromin chlorid, and therefore the employment of the latter would be commercially impracticable if means were not provided for recovering the bromin. I provide such means and recombine the bromin of the decomposed bromin chlorid with a fresh body of chlorin, so as to again form bromin chlorid. This bromin chlorid may be used upon a new supply of ore and in this way the process is practically continuous and very inexpensive, so that it is well adapted for commercial purposes.
The accompanying drawing represents an elevation, partly in section, of an apparatus for carrying my invention into effect.
The pulverized ore is placed into a revolving barrel or cylinder a, and upon it is poured a solution in water of bromin chlorid, which may be prepared by any of the well-known methods. The amount of bromin chlorid necessary to completely dissolve the gold va- Serial No. 569,035. (No specimens.)
ries considerably with the nature of the ore, but in mostinstances from about live to twenty pounds of bromin chlorid per ton of ore, and dissolved in as much water as is necessary to make an easily-owing pulp of the ore, is sufficient.
The mixture is stirred by the rotation of the barrel a for from one to three hours, when the gold will be dissolved. The dissolved gold is leached and separated from the gangue by any suitable method, and is collected in a tank h. The solution in this tank will contain the gold as well as other soluble bases which may have been present in the ore.
. These bases will exist in the form of chlorids,
they having abstracted the chlorin from the bromin chlorid, and thus set the bromin free. In order to recouvert this liberated bromin into bromin chlorid, I introduce chlorin into the solution. This chlorin may be generated in any suitable manner outside of the solution and introduced into it through pipe c, or the chlorin may be set free in the solution itself. The chlorin thus introduced or generated will at once combine with the free bromin and re-form bromin chlorid. In those cases in which the bases in the ore preponderate to such a degree that some of the bromin has also combined with them the chlorin will also set these bromin combinations free and convert the liberated bromin into the bromin chlorid.
Instead of forming the bromin chlorid in the tank h, by the introduction or generation of a fresh body of chlorin, I may set free the old chlorin from its combinations with the bases of the ores by the introduction of an oxidizing agent.
After the bromin chlorid has been formed in the tank h, as described, it must of course be separated from the auriferous solution. To this effect the liquid in the tank h is heated in any desired manner, preferably by conducting into it a current of steam, which is drawn from a suitable generator d. The steam will separate the bromin chlorid from the solution in the form of vapor, which is carried by the escaping steam through a pipe e and into the condenser f.
As the bromin chlorid is avery volatile IOO liquid, its complete separation from the solution in the tank l), by the aid of heat, may be readily effected.
The condenser f, which serves to liquidize the bromin-chlorid vapors, may be of an suitable construction, the drawing showing a Gay-Lussac tower, into which Water is admitted Yfrom pipeg. The liquidized brornin chlo rid collects in a tank h, having a vent c', that dips into a tank j, containing an alkali, to absorb any of the vapors that .may escape. Thus the bromin chlorid is in condition to be used over again upon a fresh body of ore.
After all the bromin chlorid has been expelled from the tank b the gold solution is run through a tap 7c into a precipitating-tank l, Where the gold is precipitated and recovered in any suitable manner. The rationale of this process is that as the broinin constitutes an excellent carrier for the chlorin all the beneficial effects attending the use of both these halogens may be obtained in the most economical manner. Heretofore enough chlorin could only be obtained by means of pressure, necessitatingthe use of complicated and expensive apparatus, and involving, moreover, the loss of all the chlorin used, lWhile with my improved process only so much chlorin is consumed as enters actually into combination with the bases.
The process of extracting gold from ore, which consists in dissolving the precious metals by bromin chlorid, adding chlorin to the liberated bromin, separating the bromin chlorid thus formed from the solution in the form of vapor, condensing such vapor, and precipitating the gold, substantially as specified.
Signed at New York, in the county of New York and State of New York, this lith day of November, A. D. 1895. e
BERTRAND C. HINMAN.
Witnesses:
F. v. BRIEsEN, WILLIAM SCHULZ.
US569334D Process of extracting gold Expired - Lifetime US569334A (en)

Publications (1)

Publication Number Publication Date
US569334A true US569334A (en) 1896-10-13

Family

ID=2638039

Family Applications (1)

Application Number Title Priority Date Filing Date
US569334D Expired - Lifetime US569334A (en) Process of extracting gold

Country Status (1)

Country Link
US (1) US569334A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2006200211B2 (en) * 1997-12-03 2007-03-29 Wm. Wrigley Jr. Company Improved chewing gum formulations including aspartame and sodium bicarbonate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2006200211B2 (en) * 1997-12-03 2007-03-29 Wm. Wrigley Jr. Company Improved chewing gum formulations including aspartame and sodium bicarbonate

Similar Documents

Publication Publication Date Title
US20210156003A1 (en) Recovery of metals from pyrite
US569334A (en) Process of extracting gold
Clennell The cyanide handbook
AU2010205521B2 (en) Metal recovery from metallurgical waste by chloridising
US890432A (en) Wet process of recovering antimony in a pure state from ores, concentrates, tailings, and slimes containing it.
US2017330A (en) Metallurgical process and apparatus
US1173467A (en) Process of treating zinc ores.
US568741A (en) Henry r
US1897921A (en) Production of sulphur from sulphides
US2425995A (en) Process for treating oxidized ores of zinc
US1180765A (en) Extraction of zinc from its ores or products.
US1162150A (en) Process of treating metallic ores.
US1916853A (en) Process of treating ores
US733859A (en) Process of extracting precious metals from their ores.
US704640A (en) Process of extracting copper and nickel from sulfid compounds.
US723949A (en) Process of separating copper from ores.
US702153A (en) Treatment of ores and materials containing antimony.
US587128A (en) Ernest frederick turner
US592055A (en) Process of treating ores
US984090A (en) Treatment of gold-bearing antimony ores.
US900088A (en) Treating oxid of zinc.
US656497A (en) Process of treating zinc-bearing complex ores for recovery of zinc or other metals therefrom.
US875866A (en) Process of obtaining zinc oxid from zinc ores.
US700311A (en) Treatment of complex and refractory ores.
US544499A (en) Hugo brewer