US282863A - Asstgnoes op one-halp to william a - Google Patents
Asstgnoes op one-halp to william a Download PDFInfo
- Publication number
- US282863A US282863A US282863DA US282863A US 282863 A US282863 A US 282863A US 282863D A US282863D A US 282863DA US 282863 A US282863 A US 282863A
- Authority
- US
- United States
- Prior art keywords
- vessel
- pulp
- william
- amalgamating
- grinding
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- 238000000034 method Methods 0.000 description 18
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 12
- 239000002245 particle Substances 0.000 description 10
- 238000010276 construction Methods 0.000 description 6
- 239000002184 metal Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 108060001626 set-3 Proteins 0.000 description 2
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
- B03B9/061—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/085—Subsequent treatment of concentrated product of the feed, e.g. conditioning, de-sliming
Definitions
- Our invention relates to an improved'amal gamator and process of grinding ores of the.
- I t is designed more especially for operating upon tailings orc matter that has been previously worked.
- Ourinvention is equallyadapted for the treatment of ores taken directly from the mill and not previously worked by any amalgamating and separating processes.
- Figure 1 shows the general arrangement of the apparatus which we employ for treating ores by our improved process in a continuous manner and on a large scale.
- Fig. 2 is a vertical 0 longitudinal section'through the center of the amalgamating-vessel, showing the general con-- struction of this part of our apparatus.
- Fig. 3 is an endelevation of Fig. 2, taken from the front.
- Fig. 4 is an end elevation of the set- 3 5 tling-ves'sel.
- the grinder A may be any suitable mill or grinding-pan of the kinds now in use.
- the amalgamating-vessel B we construct preferably of cylindrical shape, and of sheet 40 metal, very similar in form and structure to the shell of a steam-boiler.
- In its top we provide an inlet, 0, closed with aremovable cover, 0, and beneath its bottom we arrange a gratesurface, fire-box, and combustion-chamber.
- 4 5 We place the vesselB in abrick-work chamber, D, connected with a chimney, and provided with the usual doors and draft-openings. This is a practical, convenient, and well-known construction, requiring no particular skill to set up and manage.
- XVithin this vessel we ated from the -outside-.
- At one end of the vessel we provide'a discharge-opening controlled by a suitable shutofl' cock, J, and located just above the line reached by the body of quicksilver placed on the bottom. This outlet is'for the discharge of the pnlpfrom above the quicksilver.
- a second discharge, K, having a cock, Z, is placed 0 lower downand in position to run off the body of quicksilver when'the same is sufliciently charged with metal and required to be renewed.
- This vessel is therefore a close air and watertight cylindrical chamber, having.
- a stratum or body of quicksilver is placed on the bottom to a certain depth which is governed by the size and capacity of the vessel, and then after being supplied'with a charge of the pulp'from the grinding-mill it is tightly closed at the inlets and heat is applied by the fire beneath it;
- the grinding apparatus and the amalgamating-vessel weinterpose a receiving and supplying tank or trough, Q, for use-when the process is to be carried on in a continuous condition, asit permits the operation of grinding to proceed without interruption, While the amalgamating-vessel receives its charges at the proper intervals from the accumulating contents of the tank.
- this apparatus is operated substantially as follows:
- the amalgamator B having thefire under it, is charged with a quantity of pulp from thetank until the contents reach a point or level just above the shaft E.
- the cover 0 is then secured on and tightly sealed at the joint and the rotating shaft E is set in motion.
- the paddles orarms upon this shaft then being carried down through the pulp, bring the particles into intimate contact with the quicksilver below the pulp, and also loosen and agitate the mass, so as to permit the heavier particles to settle down through it by virtue of I their superior gravity.
- By the action of the heat also, there is effected an ebullition' or a throwing up of the quicksilver in the form of stringers?
- the charge of pulp can be settled directly in this vessel, .which will render the operations of amalgamating in such vessel intermittent; or by employing a separate vessel, R, as a settler the charges, when properly worked, can be run off each time for subsequent treatment to the settling operation, and the amalgamating-vessel can be immediately recharged from the grinder or its tank, thereby making the operation of the apparatus more nearly continuous.
- the amalgamator permit the settling operation to be rapidly and efiectively performed in this vessel by simply shutting off the heat beneath its bottom and turning in the cold water. At such times the speed of the shaft E will be reduced and the flow of cold water under pressure through the vessel will condense the vapors and produce precipitation of the heavier particles, and at the same time carry off from the vessel the light and worthless matter through the pipe N.
- This operation would be more. expensive in working on a large scale, as the interruption in the amalgamating operation would involve a loss of heat and the additional time required at the beginning of each operation to raise the heat within the vessel to the required degree. To overcome this delay and to reduce the expense, we grind the pulp with hot water, and we employ also the separate settling-vessel B.
- This is a vessel similar in its general construction to the amalgamating-vessel B, excepting steadof one discharge-outlet in the head we provide several discharges at different levels.
- This settler is a closed vessel, and has a stream a or body of cold water under pressure passed continuously through it, for which purpose the 8 5 water-inlet s and outlet t are connected with suitable pipes for the supply and discharge.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
(No Model.)
- C. H. DOW & W.-H. CHANDLER,
PROCESS OF GRINDING AND APPARATUS FOR AMALGAMATING ORES. .No. 282,863. Patented Aug. '7, 1883.
Fig. Z. Grinder .fi. I
Tank Q Amalyamaior s D, L 1' R Jeltler WAT] f /4 E v Z/E afar-5:, W 21525555 UNIT D I STATES PATENT JQFFICE...
CHARLES H. DOW AND WILLIAM H. CHANDLER, or VIRGINIA crrv, nEvAnA, ASSIGNORS or ONE-HALF TO .WILLIAM A. sunnvns, or BORDENTOVVN, ANI) MYRON L. JUSTIN, or JERSEY- CITY, New JERSEY.
PROCESS OF GRINDING AND APPARATUS FOR A MALGAMATING ORES- A SPECIFICATION forming part of Iietters Patent No. 282,863, dated August 7, 1883.
Application filed January 19. W82. (X model.) I
To all whom, it may concern.-
Be itkuown that we, CHARLES H. Dow and WVILLIAM H. CHANDLER, of Virginia City, in the county of Storey and State of Nevada,
have invented an Improved Process of Grinding and Apparatus for Am'algamating Ores; and we do hereby declare that the following is a full, clear, and exact description of our said process and of the machinery or apparatus which we have devised for successfully practicing or carrying ourinvention into effect, refer- .encebeing had to the accompanying drawings.
- Our invention relates to an improved'amal gamator and process of grinding ores of the.
precious metals after they have been crushed and are in condition to be ground and mixed with water.
I t is designed more especially for operating upon tailings orc matter that has been previously worked. c
Ourinvention is equallyadapted for the treatment of ores taken directly from the mill and not previously worked by any amalgamating and separating processes.
Referring to the accompanying drawings, Figure 1 shows the general arrangement of the apparatus which we employ for treating ores by our improved process in a continuous manner and on a large scale. Fig. 2 is a vertical 0 longitudinal section'through the center of the amalgamating-vessel, showing the general con-- struction of this part of our apparatus. Fig. 3 is an endelevation of Fig. 2, taken from the front. Fig. 4 is an end elevation of the set- 3 5 tling-ves'sel.
The grinder A may be any suitable mill or grinding-pan of the kinds now in use.
The amalgamating-vessel B we construct preferably of cylindrical shape, and of sheet 40 metal, very similar in form and structure to the shell of a steam-boiler. In its top we provide an inlet, 0, closed with aremovable cover, 0, and beneath its bottom we arrange a gratesurface, fire-box, and combustion-chamber. 4 5 We place the vesselB in abrick-work chamber, D, connected with a chimney, and provided with the usual doors and draft-openings. This is a practical, convenient, and well-known construction, requiring no particular skill to set up and manage. XVithin this vessel we ated from the -outside-.
place a horizontal shaft, E, having anumber of radial arms, f, carrying blades or paddles g {1. The blades 9 g are arranged at the outer ends of the arms f, and leave'an open space betweenthem and the shaft, throughwhich the particles earried'up by the paddles or blades can fall without being carried over. One end of this shaft is supported in a bearing inside the vessel agaiust one head, while the other end projects through the opposite head and turns in a stufling-box, h, at that point. A rotary motion is imparted to this shaft by means of the pulley I.
At one end of the vessel we provide'a discharge-opening controlled by a suitable shutofl' cock, J, and located just above the line reached by the body of quicksilver placed on the bottom. This outlet is'for the discharge of the pnlpfrom above the quicksilver. A second discharge, K, having a cock, Z, is placed 0 lower downand in position to run off the body of quicksilver when'the same is sufliciently charged with metal and required to be renewed. This vessel is therefore a close air and watertight cylindrical chamber, having. a firebox beneath it and a stirring and agitati ngdevicc withinj'itcapable of being oper- When in operation, a stratum or body of quicksilver is placed on the bottom to a certain depth which is governed by the size and capacity of the vessel, and then after being supplied'with a charge of the pulp'from the grinding-mill it is tightly closed at the inlets and heat is applied by the fire beneath it;
For regulating the temperature of the mass of pulp being treated ,in such a vessel, and also for condensing the gases and vapors therein at the end of each operation, [so as to pery, mit the cover 0 to be taken off with safety to 0 admit a fresh supply of pulp, we provide a 3 meansfor supplying a flow and circulationjof' cold water into and through the vessel in eontact with the pulp, the ,quantity and velocity 9 I of which is undereontrol. This means vcon- 5 sists of .the eold wate'r-inlet pipe M, connect- I ing with a sui ble'head to give the required pressure and thedischarge-pipe N at the opposite end of theve'ssel to lead off the over-' flow; \Ve prefer tpgcarry the end of this dis- I00 charge-pipe down into and beneath a body of water in a tank or'vessel, O, as by this means the escape of fumes'and vapors is prevented,
.and the condition and temperature of the contents of the vessel can be readily determined at any time from the water in this vessel. 1
.fOl grinding purposes.
Between. the grinding apparatus and the amalgamating-vessel weinterpose a receiving and supplying tank or trough, Q, for use-when the process is to be carried on in a continuous condition, asit permits the operation of grinding to proceed without interruption, While the amalgamating-vessel receives its charges at the proper intervals from the accumulating contents of the tank.
As thus constructed and arranged, this apparatus is operated substantially as follows: The amalgamator B, having thefire under it, is charged with a quantity of pulp from thetank until the contents reach a point or level just above the shaft E. The cover 0 is then secured on and tightly sealed at the joint and the rotating shaft E is set in motion. The paddles orarms upon this shaft, then being carried down through the pulp, bring the particles into intimate contact with the quicksilver below the pulp, and also loosen and agitate the mass, so as to permit the heavier particles to settle down through it by virtue of I their superior gravity. By the action of the heat, also, there is effected an ebullition' or a throwing up of the quicksilver in the form of stringers? from its surface into the lower part of the pulp, and the combined action of these two agenciestheheat and the stirring mechanismfacilitates aswell as insures perfect amal-' gamation. After receiving such treatment in the vessel, the charge of pulp can be settled directly in this vessel, .which will render the operations of amalgamating in such vessel intermittent; or by employing a separate vessel, R, as a settler the charges, when properly worked, can be run off each time for subsequent treatment to the settling operation, and the amalgamating-vessel can be immediately recharged from the grinder or its tank, thereby making the operation of the apparatus more nearly continuous.
The supply and circulation of cold water in that no fire is employed beneath it, and inoperation of grinding in a suitable mill, as
the amalgamator permit the settling operation to be rapidly and efiectively performed in this vessel by simply shutting off the heat beneath its bottom and turning in the cold water. At such times the speed of the shaft E will be reduced and the flow of cold water under pressure through the vessel will condense the vapors and produce precipitation of the heavier particles, and at the same time carry off from the vessel the light and worthless matter through the pipe N. This operation, however, would be more. expensive in working on a large scale, as the interruption in the amalgamating operation would involve a loss of heat and the additional time required at the beginning of each operation to raise the heat within the vessel to the required degree. To overcome this delay and to reduce the expense, we grind the pulp with hot water, and we employ also the separate settling-vessel B. This is a vessel similar in its general construction to the amalgamating-vessel B, excepting steadof one discharge-outlet in the head we provide several discharges at different levels. This settler is a closed vessel, and has a stream a or body of cold water under pressure passed continuously through it, for which purpose the 8 5 water-inlet s and outlet t are connected with suitable pipes for the supply and discharge.
By the use of this stream of water the operation of settling in an apparatus of this character is performed rapidly and effectively, and 0 it contributes-in a considerable degree to .the
successful and economical application and working of our improved process.
Having thus fully described our invention, what we claim, and desire to secure by Letters Patent, is
1. The method herein described of grinding .ore pulp, the same consisting in subjecting the pulp to the action of hot water during the I00 herein set forth.
2. In an apparatus for treating ore pulp to separate the valuable particles therefrom, the combination of the grinder and amalgamator,
connected, as described, with the furnace for heating the amalgamator, and the water-pipe passing through the said furnace and coir nected to the grinder, substantially as set forth.
Witness our hands and seals.
CHAS. H..DOW. [L. s.] WM. H. CHANDLER. [L. s.]
In presence of EDWARD E. OSBORN, D. SELLECK.
It is hereby certified that'Letters Patent No. 282,863, dated August 7, 1883, for an improvement in the Process of and Apparatus for Amalgamating Ores, were erroneously granted to Charles H. Dow, William H.- Chandler, William A. Shreves, and Myron L. Justin, as owners thereof; that it appears by assignment on record in the Patent Ofiice that said Letters Patent should have been granted to William H. Chandler, William A. Shreves and Myron L. Justin, as owners of the entire interest; and that the proper corrections have been made in the files and records pertaining to the case in the Patent Oflice, and should be read in the Letters Patent to make them conform therewith. I I
Signed, oountersigned, and sealed this 14th day of August, A. l). 1883.
M. L. JOSLYN, Acting Secretary of the Interior.
[SEAL] Gountersi gn ed E. M. MARBLE,
Commissioner of Pafents.
Publications (1)
Publication Number | Publication Date |
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US282863A true US282863A (en) | 1883-08-07 |
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US282863D Expired - Lifetime US282863A (en) | Asstgnoes op one-halp to william a |
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