US489216A - Amalgamator - Google Patents
Amalgamator Download PDFInfo
- Publication number
- US489216A US489216A US489216DA US489216A US 489216 A US489216 A US 489216A US 489216D A US489216D A US 489216DA US 489216 A US489216 A US 489216A
- Authority
- US
- United States
- Prior art keywords
- ore
- cylinders
- amalgamator
- current
- mercury
- 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
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 10
- 230000009471 action Effects 0.000 description 7
- 229910052753 mercury Inorganic materials 0.000 description 7
- 239000004020 conductor Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 3
- 229910052737 gold Inorganic materials 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- GRYSXUXXBDSYRT-WOUKDFQISA-N (2r,3r,4r,5r)-2-(hydroxymethyl)-4-methoxy-5-[6-(methylamino)purin-9-yl]oxolan-3-ol Chemical compound C1=NC=2C(NC)=NC=NC=2N1[C@@H]1O[C@H](CO)[C@@H](O)[C@H]1OC GRYSXUXXBDSYRT-WOUKDFQISA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 229910000754 Wrought iron Inorganic materials 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000005267 amalgamation Methods 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 210000004907 gland Anatomy 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 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
- C22B11/00—Obtaining noble metals
- C22B11/10—Obtaining noble metals by amalgamating
Definitions
- This invention relates to amalgamating machinery for use in the treatment of gold and silver ores, and is more especially designed for use in carrying out the process of treating ores set forth in an application filed in the joint names of Hugh Calhoun and Aron Beam, on the 1st day of April 1891, designated by Serial No. 387,275.
- the apparatus is susceptible of general application to amalgamating processes, and will be found particularly efficient in the treatment of dry ores, or those containing no base metals in quantity sufficient to form a flux.
- Figure 1 is a per- 2 5 spective view of the improved apparatus.
- Figs. 2 and 3 respectively, transverse and longitudinal vertical sections through the same.
- the apparatus consists essentially of a series of cylinders A, of wrought iron, cast iron,
- each cylinder A there is arranged an axial shaft D, the ends of which are carried through stuffing boxes or glands E, and each of which is furnished with a gear wheel F, or equivalent means of rotation.
- gear wheel F or equivalent means of rotation.
- bevel gears are preferred, and these receive motion from similar gears, G, carried by a shaft I-I, bearing a band pulley I, and receiving motion from any convenient source,
- the dimensions of the blades or paddles may vary, and their faces may be set more or less oblique to their respective planes of rotation, these matters depending somewhat upon the size of the ore particles,the condition in which the ore is delivered to the amalgamator,and like considerations. Theyshould travel quite close to the innerfaces or walls of the cylinder, which latter are stationary and serve only as receptacles or containers for the ore, the agitation and working thereof being wholly performed by the blades or paddles. It is, however, practicable to rotate both the cylinders and the shafts, or even the cylinders alone, but this is not deemed advantageous.
- the spirals of the shafts may be alternated in direction, or the shafts may be made to ro-: fate to the right and left, alternately, to cause the material to traverse the cylinders in series, and to pass from each to the next through 1 the large connecting pipes or trunks I), which as stated are placed alternately at oppositeends, as shown in Fig. 1.
- a feed hopper, 'K At the receiving end of the first cylinder of the series there is arranged a feed hopper, 'K, through which the ore and the quicksilver are. both intros cuted.
- the furnace or heater 0 may he of any convenient construction, the ordinary fire-box, grate-bars, ash pit, and doors being repre- 8 5 sented in the drawings.
- L indicates an electric generator or source of electrical energy, by which term it is meant to include any and all known forms of generator, whether galvanic, voltaic, dynamic or other, the ordinary dynamo being, however, preferred by reason of its convenience, economy, and efliciency.
- the brushes of the dynamo, or the binding posts of the generator are respectively connected with the receiving and 5 delivery ends of the first and last cylinders A, and the commutator is of such construction as to deliver a current continuous as to direction, but broken or intermittent as to duration.
- a continuous current is converted into a series of rapidly recurring pulsations or shocks,so rapid or closely succeeding as to be imperceptible to the senses though existing in fact.
- the apparatus is not dependent for its successful operation, upon the employment of electricity, but its action is materially improved thereby. Theinterruption of the current is found to be quite important.
- the ores are preferably reduced to comparatively finecondition and roasted at a heat not exceeding 1200 or thereabout, (Fahrenheit) in the pres ence of muriate of ammonia and carbon; but if not subjected to this chlorination, and if of a refractory character, should have mingled with them, per ton of ore, oxalic acid four pounds; caustic soda four pounds; sal ammoniac four pounds,-and common salt five pounds.
- the batch being thus prepared is delivered to the hopper K and thence to the cylinders, in as stiff a condition as it is practicable to handle it in,'and the mercury is run in with the ore.
- the blades or paddles turn the ore over and over,pres's it, and move it along through the cylinders, until it is finally discharged at the rear end of the last one of the series, or through an intermediate outlet at any suitable point:
- the action of the blades or paddles though easy and gentle, and closely resembling hand treatment, is peculiarly efficacious, especially with slimy ores,pressing the gold or silver out of the enveloping slime, and exposing it to the quicksilver, which promptly takes it up.
- the number, size, and arrangement of cylinders may be varied, though it is deemed advantageous to use two or more, and to make them of or about eight inches diameter, and
- the electric current thus applied both aids or eifeets chlorination, and aggregates the gold in the pure metallic state, removing the coating which otherwise wouldprevent the mer'curyfrom acting upon and taking up the particles.
- the current seems also to increase the affinity of the mercury for the gold and silver, and for these several reasons we deem it very important to employ it.
- the mercury should be thoroughly commingled with and distributed through the mass of ore, and the pulp should be brought to proper consistency before it is introduced into the amalgamator. After the ore leaves the amalgamator it should be passed into a settler, of any convenient type, to give the mercury time 'to settle, using hot water in the settler and drawing off the pulp in the ordinary way.
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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
(No Model.)
H. CALHOUN 8a A. M. BEAM.
AMALGAMATOR.
Patented Jan. 3, L893.
HUGH cALHOu/v,
ARON M BEAM TVZZ'ness as UNITED STATES PATENT OFFICE.
HUGH CALHOUN, OF HOT SPRINGS, AND ARON. M. BEAM, OF BEAR, ASSIGNORS OF ONE-THIRD TO PROSPER H. ELLSVVORTH, OF HOT SPRINGS, ARKANSAS.
AMALGAMATO R.
SPECIFICATION forming part of Letters Patent No. 489,216, dated January 3, 1893.
Application filed June 30, 1891. Serial No. 397.995. (No model.)
To all whom it may concern.-
Be it known that we, HUGH CALHOUN, residing at Hot Springs, in the county of Garland, and ARON. M. BEAM, residing at Bear,
in the county of Montgomery, State of Arkansas, citizens of the United Stat-es, have invented certain new and useful Improvements in Amalgamators, of which the following is a specification.
This invention relates to amalgamating machinery for use in the treatment of gold and silver ores, and is more especially designed for use in carrying out the process of treating ores set forth in an application filed in the joint names of Hugh Calhoun and Aron Beam, on the 1st day of April 1891, designated by Serial No. 387,275. Although especially designed for such use, the apparatus is susceptible of general application to amalgamating processes, and will be found particularly efficient in the treatment of dry ores, or those containing no base metals in quantity sufficient to form a flux.
In the annexed drawings, Figure 1 is a per- 2 5 spective view of the improved apparatus; and
Figs. 2 and 3 respectively, transverse and longitudinal vertical sections through the same.
The apparatus consists essentially of a series of cylinders A, of wrought iron, cast iron,
or other suitable material, connected alternately at opposite ends,-a tank or vessel 13 in which said cylinders are mounted; and a furnace, O, beneath the tank or vessel to heat the water with which it is supplied when the 5 apparatus is in use.
Within each cylinder A there is arranged an axial shaft D, the ends of which are carried through stuffing boxes or glands E, and each of which is furnished with a gear wheel F, or equivalent means of rotation. In practice bevel gears are preferred, and these receive motion from similar gears, G, carried by a shaft I-I, bearing a band pulley I, and receiving motion from any convenient source,
through a belt J. It is, however, apparent that any other means of rotating the shafts D may be adopted. Each shaft is armed with a series of blades or paddles a, projecting radially therefrom or substantially so,the blades being arranged in spiral order aboutthe shafts so as to constitute in each case a spiral conveyer.
The dimensions of the blades or paddles may vary, and their faces may be set more or less oblique to their respective planes of rotation, these matters depending somewhat upon the size of the ore particles,the condition in which the ore is delivered to the amalgamator,and like considerations. Theyshould travel quite close to the innerfaces or walls of the cylinder, which latter are stationary and serve only as receptacles or containers for the ore, the agitation and working thereof being wholly performed by the blades or paddles. It is, however, practicable to rotate both the cylinders and the shafts, or even the cylinders alone, but this is not deemed advantageous. The spirals of the shafts may be alternated in direction, or the shafts may be made to ro-: fate to the right and left, alternately, to cause the material to traverse the cylinders in series, and to pass from each to the next through 1 the large connecting pipes or trunks I), which as stated are placed alternately at oppositeends, as shown in Fig. 1. At the receiving end of the first cylinder of the series there is arranged a feed hopper, 'K, through which the ore and the quicksilver are. both intros duced. At or near the midlength of each cyl-' inder, and at other points if deemed advis- 8o able, are sight doors 0, to permit inspection of the batch from time to time. H
The furnace or heater 0 may he of any convenient construction, the ordinary fire-box, grate-bars, ash pit, and doors being repre- 8 5 sented in the drawings.
L indicates an electric generator or source of electrical energy, by which term it is meant to include any and all known forms of generator, whether galvanic, voltaic, dynamic or other, the ordinary dynamo being, however, preferred by reason of its convenience, economy, and efliciency. The brushes of the dynamo, or the binding posts of the generator are respectively connected with the receiving and 5 delivery ends of the first and last cylinders A, and the commutator is of such construction as to deliver a current continuous as to direction, but broken or intermittent as to duration. In other words, what is commonly termed a continuous current, is converted into a series of rapidly recurring pulsations or shocks,so rapid or closely succeeding as to be imperceptible to the senses though existing in fact. To render the current efficacious and prevent its being short circuited it is of course necessary that the cylinders be thoroughly insulated from the tank, or that the latter be made of non-conducting material,and similar protection is to be made against short-circuiting through shaft H.
The apparatus is not dependent for its successful operation, upon the employment of electricity, but its action is materially improved thereby. Theinterruption of the current is found to be quite important.
When using the apparatus, the tank or ves-- sel B is supplied with water to a depth sufficient to about two-thirds cover the cylinders A, and fire is started in the furnace and kept up to maintain the water at or near the boiling point,the heat thereby imparted to the contents of the cylinders being thus kept quite uniform, and serving to quicken and enhance the action of the quicksilver. The ores, particularly if of the character mentioned, are preferably reduced to comparatively finecondition and roasted at a heat not exceeding 1200 or thereabout, (Fahrenheit) in the pres ence of muriate of ammonia and carbon; but if not subjected to this chlorination, and if of a refractory character, should have mingled with them, per ton of ore, oxalic acid four pounds; caustic soda four pounds; sal ammoniac four pounds,-and common salt five pounds. The batch being thus prepared is delivered to the hopper K and thence to the cylinders, in as stiff a condition as it is practicable to handle it in,'and the mercury is run in with the ore. The blades or paddles turn the ore over and over,pres's it, and move it along through the cylinders, until it is finally discharged at the rear end of the last one of the series, or through an intermediate outlet at any suitable point: The action of the blades or paddles though easy and gentle, and closely resembling hand treatment, is peculiarly efficacious, especially with slimy ores,pressing the gold or silver out of the enveloping slime, and exposing it to the quicksilver, which promptly takes it up.
The action of the electric current materially expedites and improves the work, particularly with certain classes of ores, but its use is not essential. I
The number, size, and arrangement of cylinders may be varied, though it is deemed advantageous to use two or more, and to make them of or about eight inches diameter, and
ten feet in length,with removable heads to facilitate repair, or access to the interior.
It is found advisable to employ a current of from sixteen to eighteen volts, and of about thirty five amperes, and to break the same about two thousand five hundred times per minute, which may readily be accomplished by leaving proper spaces between the conducting strips of the commutator cylinder, or by means of an intermediate current breaker between the generator and the amalgamator. It is also found advantageous to employ a conductor of large capacity from the generator to the amalgamator, and one of comparatively small capacity for the return from the amalgamator to the commutator, as by this plan the electricity passes freely to the ore' or charge and there acts efficaciously,the ore apparently -serving or acting as a condenser,'while the comparatively small conducting capacity of the return line tends to more effectually hold the electric current back and cause it to permeate the entire mass of ore. Whether this be or be not the correct theory of action,'practice demonstrates that it is highly advantageous both to interrupt the current and to employ a return conductor relatively smaller than the supply conductor. The electric current thus applied, both aids or eifeets chlorination, and aggregates the gold in the pure metallic state, removing the coating which otherwise wouldprevent the mer'curyfrom acting upon and taking up the particles. The current seems also to increase the affinity of the mercury for the gold and silver, and for these several reasons we deem it very important to employ it. The mercury should be thoroughly commingled with and distributed through the mass of ore, and the pulp should be brought to proper consistency before it is introduced into the amalgamator. After the ore leaves the amalgamator it should be passed into a settler, of any convenient type, to give the mercury time 'to settle, using hot water in the settler and drawing off the pulp in the ordinary way.
Ore which has been previously chlorinated may be treated in the amalgamator without fear of contaminating the mercury with lead, for the reason that in the chlorinating operation the lead becomes blackened or oxidized, the coating thus formed preventing the mercury from acting upon the lead. The electric current seems also to retard or prevent the action of the mercury upon the lead.
The invention being thus described, what is claimed is:
1. In combination with an amalgamating vessel, an electric generator connected therewith and adapted to deliver an interrupted current of constant direction. I
2. The herein-described amalgamating apparatus, consisting of connected cylinders A action of aninterrupted currentof electricity provided with spirally-bladed axial shafts; of constant direction. tank B, furnace 0, electric generator L, all In witness whereof We hereunto set our gomllfined and operating substantially as set hands in the presence of two Witnesses.
5 ort 3. The method of amalgamation herein set HUGH CALHOUN. forth, which consists in mingling with the ARON. M. BEAM. pulp a proper quantity of mercury and stir- Witnesses: ring the mass in a suitable receptacle sub- E. O. BEAM,
:0 ject to the heat of a Water bath, and to the J. A. BENNETT.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US489216A true US489216A (en) | 1893-01-03 |
Family
ID=2558062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US489216D Expired - Lifetime US489216A (en) | Amalgamator |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US489216A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2733202A (en) * | 1956-01-31 | Electrolytic cells |
-
0
- US US489216D patent/US489216A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2733202A (en) * | 1956-01-31 | Electrolytic cells |
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