US347867A - Gold separator - Google Patents
Gold separator Download PDFInfo
- Publication number
- US347867A US347867A US347867DA US347867A US 347867 A US347867 A US 347867A US 347867D A US347867D A US 347867DA US 347867 A US347867 A US 347867A
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- United States
- Prior art keywords
- bed
- ore
- separator
- pockets
- gold
- 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
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- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 title description 36
- 229910052737 gold Inorganic materials 0.000 title description 36
- 239000010931 gold Substances 0.000 title description 36
- 239000000463 material Substances 0.000 description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 42
- 239000011159 matrix material Substances 0.000 description 34
- 239000010970 precious metal Substances 0.000 description 32
- 230000005484 gravity Effects 0.000 description 24
- 238000010276 construction Methods 0.000 description 18
- 229940108928 Copper Drugs 0.000 description 14
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 14
- 229910052802 copper Inorganic materials 0.000 description 14
- 239000010949 copper Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 14
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 10
- 239000002245 particle Substances 0.000 description 10
- 238000005267 amalgamation Methods 0.000 description 8
- 239000000428 dust Substances 0.000 description 8
- 230000000717 retained Effects 0.000 description 8
- 238000000926 separation method Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 6
- 229910052753 mercury Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000004927 clay Substances 0.000 description 4
- 229910052570 clay Inorganic materials 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000001788 irregular Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000001105 regulatory Effects 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 229910000497 Amalgam Inorganic materials 0.000 description 2
- 241000430525 Aurinia saxatilis Species 0.000 description 2
- 210000000936 Intestines Anatomy 0.000 description 2
- 241001584775 Tunga penetrans Species 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 235000014987 copper Nutrition 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000002349 favourable Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002923 metal particle Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000010454 slate Substances 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
- B03B4/00—Separating by pneumatic tables or by pneumatic jigs
Definitions
- Figure 1 is a longitudinal vertical sectionof a machine embodying myinvention on the line 1 1, Fig. 2.
- Fig. 2 is a top view of the same, the dust slide or cover being removed i -to show the-interior.
- Fig. 3 is a transverse section on the line 33, Fig. 2.
- Fig. 4 is a vertical section on the line 4 4, Fig.
- Fig. 5 is a perspective view of a portion of one of the perforated steel plates for forming the pockets.
- Fig.6 is a side ele-. vation of the same.
- Fig. 7 is a detail showing the means for imparting a lateral vibratory movement to the separator or pocket-cham- 'ber.
- Fig. 9 is a longitudinal section of a modification, adapting the separator to use water instead of air.
- Fig. 10 is a transverse section of the same on theline 1010, Fig.
- FIGS. 11 and 13 show previous constructions of perforated pockets which have proved defective.
- Figs. 12 and 14 show steps of the construction devised by me to overcome the 5 deficiencies of the pockets shown in Figs. 11
- My present invention relates to the construction and operation of gravity-separators forrecovering or obtaining the precious metals from their earthy matrices.
- Fig. 8 is a top or plan view of the ma -by gravity,: or is taken up by the quicksilver while the gangue is floated off.
- the jigger operates by causing the pulsationof water througha perforated trough or screen, 5 so as'to permit the heavier precious metal to be concentrated or sink through the screen into the trough or water-box, while the matrix passes off the screen out of the machine.
- an airblast is substituted for water to produce the pulsations which shall cause the separation of the metal and matrix and permit the heavier precious metal to fall through the screen or separator into the air-box, while the earthy matter or gangue passes off of the screen, as in the wet process.
- the precious metal may The sieve or perbe present in the condition of flour, scale, flake, shot, nugget, or common gold-dust in matrices of clay, sand. adobe clay, gravel, decomposed rock, and earthy matter, hard-pan, black sand, iron pyrites, slate, &c., or in any conceivable mixture of any or all of these. It is also well understood that the force of the downward movement of the particles under treatment will under these circumstances vary according to their volumes or according to the cubes of their relative dimensions, while the resistance will vary as their exposed surfaces or the squares of their dimensions.
- the object of the present invention is to overcome the several disadvantages hereinbefore specified, and provide means adapted to separate and retain all or substantially all the precious metal without regard to its character or condition or the nature of the matrix.
- the interposed mobile permeable mass must be maintained of uniform depth or thickness throughout, in order to maintain uniformity of operation and effectiveness.
- the resistance to the upward passage of the air (or water) must be greater in the interstices of the interposed permeable mass (ore-bed) than in its passage through the stratum'of earth under treatment.
- A indicates a frame-work adapted to support the hopper B, the separator G, and suitable mechanism for vibrating the separator 0.
- the hopper B in the present instance, is provided with a gate or slide, 6, and the mechanism shown for vibrating or rocking the separator consists of the shaft D, with crank-pin D and link-rod D pivoted to the separator C, so as to vibrate the separator laterally instead of longitudinally, as usual.
- the special construction of the aforesaid devices is, however, immaterial, as they form no part of the present invention, and may be of any desired character.
- the gist of the present invention lies in the construction and operation of the separatorO.
- 0 indicates the side walls of the separator; E, the ore-bed, and c' the (air or water) chamber below the ore-bed.
- the ore-bed E is preferably formed of a series of pockets, 0, arranged close together in step form, or one slightly lower than the other, to form an incline which facilitates the dis charge of the refuse earthy matter or gangue,
- the inclines or inclined tables e are preferably about the width of the pockets, though they may be narrower, their value being measurably proportioned to their width.
- the alternate pockets 0 and inclines e divide the bed up into portions where the material is subjected to vibration only, and portions where it is subjectedto vibration and air or water currents; consequently the fine gold has a chance to gravitate or sink more rapidly than the lighter fine particles of matrix while passing over the inclines, and as a consequence the line gold will more readily remain in the pocket,while the line matrix, being acted upon by the current, will pafi or flow toward the tail of the saparator.
- These pocketse which extend transversely of the machine,have pervious bottoms, to permit the upward flow of. a current of air or water from the chamber 0', and are preferably constructed from slotted Ill) notwithstanding the vibration of the ore-bed.
- Fig. 5 steel plates, as shown in Fig. 5, butmay be of wire netting or gauze or any suitable pervious material.
- a dead-plate or dead-block, 6 At each end of the pocket 6 is provided a dead-plate or dead-block, 6 to prevent the current from chamber 0 crossing the ends of the pockets 6, (see Fig. 14.) and this or equivalent construction should be adopted in order to confine the current to such portions of the pocket as present an ore-bed of uniform depth and resistance to the current.
- Figs. 14 this or equivalent construction should be adopted in order to confine the current to such portions of the pocket as present an ore-bed of uniform depth and resistance to the current.
- each pocket e Just over the ore-bed, opposite the ends of each pocket e, are placed angleirons or deflcclors e, which turn or direct the earth unjl er treatment from the dead-plate e, and side walls over or back on the operative face of the ore-bed, so that none of the earth shall pass the bed without thorough treatment.
- any loose material of uni-- form size, of specific gravity intermediate between the precious metal and matrix, and of a size which will afl'ord a resistance to the air or water current greater than the resistance of the matter to be treated, may be employed 1 to fill the'pockets' e and form the ore'bed; but
- the chamber a Beneath the-ore-bed is the chamber a, which will be either an air or water chamber, according as the upward current through the orebed is to be air or water.”
- air is preferred, as water is not always obtainable in the quantities. desired, and in such case the chamber 0 is provided with a valved port, 0 from which a flexible conduit, 0, leads to a suitable fan or blower for creating anair blast.
- a I 0 indicates a valve arranged in the port and operated by a screw, c, or its equivalent, whereby the size of port 0 may be varied to obtain the desired volumeand pressure of the air-current.
- d indicates a small safe or strong box, (which should be locked,) connected with thelowest part ot'the chamber by a suitable flexible pipe, d, though, if desired, the box d may be secured directly to the floor of chamber 0.
- each pocket e may have its individual well W, (see Figs. 9 and 10,) which extends upon each side of the orebed E. as at w, and is supplied by a flexible pipe,P,havingavalve,p-apipe on each sideby which means the vibration of the ore-bed will not'interfere wit-h the steady constant flow of the current, so desirable in this class of machines.
- the lower ends of the flexible pipes P are submerged in the water of the side chambers, to, to prevent the formation of airbubbles,which, if driven down under and permitted to rise through the ore-bed and earthy matter,would seriously interfere with the sn'ccessful operation of the machine;
- F indicates the dust-chamber above the ore-bed; f, the discharge thereof,'whence the gangue or refuse escapes; G: the receiving table which receives the material to be treatedin a pulverized condition from the hopper B, which is placed. over the feed-openingg of the separator; and H indicates a. pendent diast the escape of dust and air at the head of the separator, v
- the cover I of the dust-chamber F is arranged as a slide, cut away at the feed-- opening 9, and secured by a lock, 5.
- Fig.6; or any equivalent well-known means of removably securing the dust-cover may be adopted.
- the pockets 6 having been filled with material of the character and relative specific gravity hereinbefore specified, and of 'a. size adapted to offer the specified resistance to the passage of the air or water current, or, in other words, the ore-bed E being properly prepared, the valve (0 or p, as the case may be,) is adjusted to obtain a current of the volume and pressure best adapted to the material under treatment.
- the said material in a pulverized condition, is then fed from the hopper B, through feed-opening g, upon the table G.
- the separator G will have a lateral vibration imparted to it from shaft D and crank-pin D through link or rod D", or in any other suit-able manner.
- the vibration of the separator C will cause the material under treatment to pass under diphragm Hand flow in a thin sheet or stratum over ore-bed E, where it meets the current of air or water flowing up through the ore-bed, and as the resistance is less in the strata of earth than it is in the bed, the earth strata will be so agitated that the separation of the precious metal firom the matrix will take placeabove the orebed, and the precious'mctal will by gravity sink into the ore-bed and be retained therein,
- the lateral vibration of the separator causes the intestine movement in the material in the pockets or ore-bed. and this favors the descent to the bottom of the pockets of the finer particles of precious metal,and thus effectually prevents loss by the same be ing carried off in the gangue.
- the lateral vibration of the separator combined with the upfiow of the air divided into minute jets by the ore bed through which it passes, tend not only to lift the material and overcomeits specific gravity, but also to divide particle from particle, thus reducing the whole mass into the most favorable condition'fo'r permitting the component parts to arrange themselves according to their respective specific gravities. In other words, an artificial quieksand is produced. Only the very finest dust can possibly sift into the chamber 0', and this, which is a very small per cent. of the yield. will collect in the safe or strong box d, as before specified.
- the value of the dead-block e" and dead-plate a will be more apparent than at first.
- the bulk, orsnbstautially all, of the yield will be retained in the ore-bed, so that there is .a resemblance to the amalgamating process.
- the separator 0 maybe detached from the frame, the slide I or dnst'chamber cover nulocked and removed for cleaning up. and all the precious metal recovered from the bed material, after which the material may be replacedin the pockets, and the dust-chamber cover I replaced and locked.
- a separator In a separator, a seriesof pockets containing loose material forming an ore-bed and provided with dead-blocks arranged to deflect the current from the sides of the bed or ends of its pockets, substantially as and for the pur- 3.
- a separator In a separator; a series of pockets containing loose material forming an ore-bed, and
- dead-blocks at the bottom and dead-plates at the top of the bed, arranged to form blind-pockets, which confine the mate rial and prevent the passage of currents subva-pervious bottom, dead-blocks at itsends,
- a separator-pocket for an ore-bed said pocket having a dead-block at each end near the-bottom, and a dead plate or flange extending around the pocketvat or near the level or top surface of the ore-bed, substantially as and for the purposes specified.
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
(No Model.) 4 Sheets-Sheet 1 W. L. CARD.
GOLD SBPARATOR.
Patented Aug. 24, 1886-.-
(No Mode1.) W L CARD 4Sheets-S11eet2.
' GOLi) sfiPAnAToie. I No. 347,867. Patented Aug. 24,- 1886. i v (WI Mu H W, III) 1 F' W L (No Model.) 4 Sheets-Sheet :3.
' W. L. CARD.
GOLD SEPARATOR. No. 347,867. Patented Aug. 24, 1886.
- .fjz' gd,
4 Sheets Sheet 4.
(No Model.)
W. L. CARD.
GOLD SEPARATOR.
N0. 347,867. Patented Aug. 24, 1886.
WILLIAM L. CARD, OF LA CROSSE, WISCONSIN, ASSIGNOR TO THE TIERR-A SEGA MINING COMPANY.
GOLD-SEPA RATO R.
SPECIFICATION forming part of Letters'Patent No. 347,867, dated August 24, 1886. v Application filed March 26, 1886. Serial No. 196,732. No model.)
To all whom it may concern:
Be it known that I, WILLIAM L. CARD, a citizen of the United States, residing at La Orosse, in the county of La Crosse and State of Wisconsin, haveinvented certain new and useful Improvements in Gold-Separators; and I hereby declare the following to be a full, clear, and exact description ofthe same, reference being had to the accompanying drawings, where- IO in Figure 1 is a longitudinal vertical sectionof a machine embodying myinvention on the line 1 1, Fig. 2. Fig. 2 is a top view of the same, the dust slide or cover being removed i -to show the-interior. Fig. 3 is a transverse section on the line 33, Fig. 2. Fig. 4 isa vertical section on the line 4 4, Fig. 3, giving an enlarged transverse view' of the pocketsof the separator. Fig. 5 is a perspective view of a portion of one of the perforated steel plates for forming the pockets. Fig.6 is a side ele-. vation of the same. Fig. 7 isa detail showing the means for imparting a lateral vibratory movement to the separator or pocket-cham- 'ber.
chine, the hopper. which is shown in Fig. 6, being omitted. Fig. 9 is a longitudinal section of a modification, adapting the separator to use water instead of air. Fig. 10 is a transverse section of the same on theline 1010, Fig.
9. Figs. 11 and 13 show previous constructions of perforated pockets which have proved defective. Figs. 12 and 14 show steps of the construction devised by me to overcome the 5 deficiencies of the pockets shown in Figs. 11
and 13. Figs. 15, 16, and 17 show the perfected and preferred forms of pockets. Like letters refer to like parts wherever they occur. I
My present invention relates to the construction and operation of gravity-separators forrecovering or obtaining the precious metals from their earthy matrices.
In'order that the objects and operation of 5 my invention may be more fully comprehended and appreciated, it will be desirable to briefly review the prior state of the art and consider in a general way the existing difiiculties and disadvantages, as well as their causes The most common processes are the amal- Fig. 8 is a top or plan view of the ma -by gravity,: or is taken up by the quicksilver while the gangue is floated off. No process has, so far as I am aware, ever been devised 'for the successful employment of a dry amalgamation process, first, because when the mer 6o cury is exposed to the air its surface at once becomes coated with a thin gray film of oxide, which prevents amalgamation, and, secondly, because of the loss of large'quantities of floured mercury. This process also demands the use of large quantities of quicksilver not readily obtained and the subsequent treatment of the amalgam to separate the metal and recover the mercury. In the second or wet process, of which the pan and cradle are'types, what are termed jiggersl are most commonly employed to economize water, which is scarce and difiic'ult to procure in many localities. The jigger operates by causing the pulsationof water througha perforated trough or screen, 5 so as'to permit the heavier precious metal to be concentrated or sink through the screen into the trough or water-box, while the matrix passes off the screen out of the machine. In the third or dry process an airblast is substituted for water to produce the pulsations which shall cause the separation of the metal and matrix and permit the heavier precious metal to fall through the screen or separator into the air-box, while the earthy matter or gangue passes off of the screen, as in the wet process. The change from water-to air as a medium for causing the pulsatipnsnecessitates other changes well known and not necessary to mention here. forated table alone being inetficient, as early as 1860 a stratum of fine gravel or like material, the gravity of which should be less than the heaviest material which was to pass through sieve and greater. than the matrix or gangue, 5 was placed on the sieve to act as valves, retard the downfiow of the water, and allow of time for the separation of the metal and matrix by the action of gravity.
The varied character of the matrix and conrec dition of the precious metal are well understood. -For instance, the precious metal may The sieve or perbe present in the condition of flour, scale, flake, shot, nugget, or common gold-dust in matrices of clay, sand. adobe clay, gravel, decomposed rock, and earthy matter, hard-pan, black sand, iron pyrites, slate, &c., or in any conceivable mixture of any or all of these. It is also well understood that the force of the downward movement of the particles under treatment will under these circumstances vary according to their volumes or according to the cubes of their relative dimensions, while the resistance will vary as their exposed surfaces or the squares of their dimensions. It will therefore be apparent that the only manner by which the present separators or concentrators can bemade to operate is by using such an impulse or upward blast as will permit the very finest gold to fall, and by allowing allthe precious metal to pass through the sieve or perforated bed into the air or water box, and if this is done then much ofthe matrix will also follow. Besides, the machine is necessarily so exposed that it can be readily robbed by the workmen. Again, if the material operated on becomes packed or unevenly distributed. over resistance to the upward flow of the air or water is irregular in its force, so that, the separation must necessarily be irregular and imperfect, and at times the fine gold may be floated off with the gangue or earthy matter.
From the above and other causes well understood by the skilled operator the larger part of the present known separators have proved failures, while none yet devised meet the requirements of the art or can be economically employed.
The object of the present invention is to overcome the several disadvantages hereinbefore specified, and provide means adapted to separate and retain all or substantially all the precious metal without regard to its character or condition or the nature of the matrix.
As a result of long and careful experiments and observation, I have discovered that in order to make a separator thorough and effective, and accomplish the objects set forth above, the following conditions must be created and maintained:
First. There must beinterposed between the medium which gives theimpulse (whetherthe same be air or water) and the material to be separated (or precious metal and its matrix) a mobile permeable mass or strata, which will not only permit the passage of the air or fluid, but will receive and retain the precious metal. For this purpose any loose materialsuch as fine, heavy, sifted, and sized gravel or shot, or any like material which is substantially lighter than gold and heavier than the matrix or earthy matter-may be used, and for this purpose I have found that copper shot is the best, first, because of its relative specific gravity; and, secondly, because it is lessliable to deface the gold and is more durable than lead shot, which is my second choice.
Second. The interposed mobile permeable mass must be maintained of uniform depth or thickness throughout, in order to maintain uniformity of operation and effectiveness.
Third. The size of its individual particles must be'regulated according to the resistance to passage of blast or water required, the coarser the material the less the resistance, and vice versa.
Fourth. The resistance to the upward passage of the air (or water) must be greater in the interstices of the interposed permeable mass (ore-bed) than in its passage through the stratum'of earth under treatment.
' I will now proceed to describe more specifically the best means known to me for earrying out my invention in order that others skilled in the art to which it appertains may apply the same.
In the drawings, A indicates a frame-work adapted to support the hopper B, the separator G, and suitable mechanism for vibrating the separator 0.
The hopper B, in the present instance, is provided with a gate or slide, 6, and the mechanism shown for vibrating or rocking the separator consists of the shaft D, with crank-pin D and link-rod D pivoted to the separator C, so as to vibrate the separator laterally instead of longitudinally, as usual. The special construction of the aforesaid devices is, however, immaterial, as they form no part of the present invention, and may be of any desired character.
The gist of the present invention lies in the construction and operation of the separatorO.
0 indicates the side walls of the separator; E, the ore-bed, and c' the (air or water) chamber below the ore-bed.
The ore-bed E is preferably formed of a series of pockets, 0, arranged close together in step form, or one slightly lower than the other, to form an incline which facilitates the dis charge of the refuse earthy matter or gangue,
said pockets being separated by inclines e,
which materially assist the precipitation, loosen up the earthy matter, and increase the capacity of the machine for handling the dirt. The inclines or inclined tables e are preferably about the width of the pockets, though they may be narrower, their value being measurably proportioned to their width. The alternate pockets 0 and inclines e divide the bed up into portions where the material is subjected to vibration only, and portions where it is subjectedto vibration and air or water currents; consequently the fine gold has a chance to gravitate or sink more rapidly than the lighter fine particles of matrix while passing over the inclines, and as a consequence the line gold will more readily remain in the pocket,while the line matrix, being acted upon by the current, will pafi or flow toward the tail of the saparator. These pocketse, which extend transversely of the machine,have pervious bottoms, to permit the upward flow of. a current of air or water from the chamber 0', and are preferably constructed from slotted Ill) notwithstanding the vibration of the ore-bed.
steel plates, as shown in Fig. 5, butmay be of wire netting or gauze or any suitable pervious material. At each end of the pocket 6 is provided a dead-plate or dead-block, 6 to prevent the current from chamber 0 crossing the ends of the pockets 6, (see Fig. 14.) and this or equivalent construction should be adopted in order to confine the current to such portions of the pocket as present an ore-bed of uniform depth and resistance to the current. In order to make this feature more apparent, Figs. 11 and 12 have been added to the drawings, showing prior forms, audit will be at once apparent that the vibrations of the ore-bed will disturb the resisting strata so much at theends of the pocket that the current, meeting less resistance and having greater velocity or force, will carry up and 011' the finer particles of the metal and matrix. To obtain the best results it is desirable to provide an upper dead-plate or flange, e", at or near the top of each and of the pocket e or ore-bed, (see Fig. 15,) to form a blind-pocket, e, which may be rounded out, as at c if desired, (see Figs. 16 and 17,) and said deadj' plate or flange e may extend entirely arourd the pocket e, (see Figs. 2, 3, and 4,) or, in other words. the pocket may have a deadplate, not only at the ends, as shown at 6 Fig. 3,butalso on both sides of the pockets, as shown at c, Fig. 4. i
It will be evident that if the above or equivalent construction ,is adopted that the strata or ore-bed through which the current passes must remain uniform throughout its extent,
This, however, will not necessarily be the result when the upper dead-plate or flange, e,
'isused alone or without an equivalent for dead block 6', as will, appear on reference to Fig. 12, which, as stated, has been introduced a for purposes of illustration.
Just over the ore-bed, opposite the ends of each pocket e, are placed angleirons or deflcclors e, which turn or direct the earth unjl er treatment from the dead-plate e, and side walls over or back on the operative face of the ore-bed, so that none of the earth shall pass the bed without thorough treatment.
Having specified the preferred construction .for the bed-pock ets, it next becomes necessary to specify the character of the ore-bed. As
hereinbefore stated, any loose material of uni-- form size, of specific gravity intermediate between the precious metal and matrix, and of a size which will afl'ord a resistance to the air or water current greater than the resistance of the matter to be treated, may be employed 1 to fill the'pockets' e and form the ore'bed; but
I prefer coppershot forthe following reasons: It is hard and durable, andwill not deface the gold, (astwould lead shot.) can be obtained and will remain ofiuniform' size and of any dcsired'size, and its gravity with relation to the usual matrix is as eight to two, and with relation to the gold as eight to nineteemwhich character, the pockets e are filled to constitute the ore-bed which is to rereive'and re -tain'the precious metal, and the size of said material is adapted to the resistance of the passage of the current desired in the ore-bed.
Beneath the-ore-bed is the chamber a, which will be either an air or water chamber, according as the upward current through the orebed is to be air or water." Of course air is preferred, as water is not always obtainable in the quantities. desired, and in such case the chamber 0 is provided with a valved port, 0 from which a flexible conduit, 0, leads to a suitable fan or blower for creating anair blast. a I 0 indicates a valve arranged in the port and operated by a screw, c, or its equivalent, whereby the size of port 0 may be varied to obtain the desired volumeand pressure of the air-current. By means of this valve and the selected material for the ore bed the force of the current of air may be regulated exactly.
d indicates a small safe or strong box, (which should be locked,) connected with thelowest part ot'the chamber by a suitable flexible pipe, d, though, if desired, the box d may be secured directly to the floor of chamber 0.
As before stated, almost all, if not all, the
gold will will be retained in the ore-bed, and
its only in extraordinary cases that the gold will be fine enough to sift into the air-chamber; but, as it ispossible for a small percent' age of the whole product to'be fine enough to sift into the chamber 0', I have provided a means forsecuri ng it against interference from the workmen.
Where water is available,and it is desirable to use it instead of a blast, each pocket e may have its individual well W, (see Figs. 9 and 10,) which extends upon each side of the orebed E. as at w, and is supplied by a flexible pipe,P,havingavalve,p-apipe on each sideby which means the vibration of the ore-bed will not'interfere wit-h the steady constant flow of the current, so desirable in this class of machines. The lower ends of the flexible pipes P are submerged in the water of the side chambers, to, to prevent the formation of airbubbles,which, if driven down under and permitted to rise through the ore-bed and earthy matter,would seriously interfere with the sn'ccessful operation of the machine;
F indicates the dust-chamber above the ore-bed; f, the discharge thereof,'whence the gangue or refuse escapes; G: the receiving table which receives the material to be treatedin a pulverized condition from the hopper B, which is placed. over the feed-openingg of the separator; and H indicates a. pendent diast the escape of dust and air at the head of the separator, v
'.-phragm'which separates the receiving-table G- ,from the dust-chamber F,--a'nd tends to pre- As'beforespecifiedmne important feature sift through the ore-bed, I have provided the strong box d; but as substantially all of the valuable matter is retained in the ore-bed, (from which it is taken in cleaning up,) it is necessary to guard this ore-bed E, which is done as follows: The feed'openingg is guarded by a series of rods or bars, 9, and the discharge end f is likewise guarded by a series of rods or bars, f, at such distances apart that while not interferring with the work of the machine they will, nevertheless, prevent the introduction of the hand or any instrument, by means of which the ore-bed F could be tampered with. These bars or rods gf will also serve to brace and strengthen the separator without materially adding to its weight or cost of construction.
In order to obtain access to the ore bed legitimately, the cover I of the dust-chamber F is arranged as a slide, cut away at the feed-- opening 9, and secured by a lock, 5. Fig.6; or any equivalent well-known means of removably securing the dust-cover may be adopted.
If the separator is tampered with, the gold can only be obtained by removing the shot or loose material which fills the pocket. and if this is removed the pockets cannot be properly refilled until the locked sliding cover is removed to expose the separator-pockets fully, consequently any tampering with the machine will be positively detected Having now poi ntcd out the preferred construction, I will describe the manner in which I operate the machine.
The pockets 6 having been filled with material of the character and relative specific gravity hereinbefore specified, and of 'a. size adapted to offer the specified resistance to the passage of the air or water current, or, in other words, the ore-bed E being properly prepared, the valve (0 or p, as the case may be,) is adjusted to obtain a current of the volume and pressure best adapted to the material under treatment. The said material, in a pulverized condition, is then fed from the hopper B, through feed-opening g, upon the table G. The separator G will have a lateral vibration imparted to it from shaft D and crank-pin D through link or rod D", or in any other suit-able manner. The vibration of the separator C will cause the material under treatment to pass under diphragm Hand flow in a thin sheet or stratum over ore-bed E, where it meets the current of air or water flowing up through the ore-bed, and as the resistance is less in the strata of earth than it is in the bed, the earth strata will be so agitated that the separation of the precious metal firom the matrix will take placeabove the orebed, and the precious'mctal will by gravity sink into the ore-bed and be retained therein,
allowing the gangue or refuse to flow freely from the bed and out at the discharge f of the separator. The lateral vibration of the separator causes the intestine movement in the material in the pockets or ore-bed. and this favors the descent to the bottom of the pockets of the finer particles of precious metal,and thus effectually prevents loss by the same be ing carried off in the gangue. The lateral vibration of the separator, combined with the upfiow of the air divided into minute jets by the ore bed through which it passes, tend not only to lift the material and overcomeits specific gravity, but also to divide particle from particle, thus reducing the whole mass into the most favorable condition'fo'r permitting the component parts to arrange themselves according to their respective specific gravities. In other words, an artificial quieksand is produced. Only the very finest dust can possibly sift into the chamber 0', and this, which is a very small per cent. of the yield. will collect in the safe or strong box d, as before specified.
On reference to Figs. 11 to 17 the value of the dead-block e" and dead-plate a will be more apparent than at first. The bulk, orsnbstautially all, of the yield will be retained in the ore-bed, so that there is .a resemblance to the amalgamating process. At the close of work the separator 0 maybe detached from the frame, the slide I or dnst'chamber cover nulocked and removed for cleaning up. and all the precious metal recovered from the bed material, after which the material may be replacedin the pockets, and the dust-chamber cover I replaced and locked.
It is evident that copper shot will, if used as material for the ore-bed, greatly facilitate cleaning up, as an incline can be used to separate the round shot from the dust, scale. and other-irregular forms of precious metal. It is also evident that the proper preparation of the ore bed E 'or distribution of the shot or like material in pockets e necessitates unobstructed access to the ore-bed, and therefore the ore-bed cannot be tampered with by the workmen without being at once discovered.
Among the advantages? of my present invention are the thorough manner in which the machine is protected against robbery; the efiective manner in which the volume and force of the. current through the machine can be controlled; the perfect manner in which the uniform depth of the ore-bed and the force of its resistance to the current can be maintained; and, finally, the capacity of the machine to recover all grades or sizes of the precious metal, and from any or all kinds of matrix, no matter how widely these. may vary in the material under treatment.
I do not herein claim the method set forth and involved, as the same forms the subjectmatter of a separate application of even date herewith, Serial No. 196,734.
I am aware that in saving gold by amalga mation, amalgamated copper cylinders and balls have been used to facilitate the coating of the gold with mercury, and do not herein claim copper balls, &c'., when amalgamated and so usetL'as the amalgamation of the cop per or other ni'etal ball would render it in a great measure unfitted for usein my machine. Myv reason for using copper shotis because the gravity of the copper shot comes nearest to equally dividing the difference in gravity I between gold and its matrix.
Having thus described my invention. What I claim,-and desire to secure by Letters Patent, 1s
1. In a separator, an ore-bed composed of a series of pockets separated by inclines. sub stantiallyas and for the purposes specified.
;.' -2.' In a separator, a seriesof pockets containing loose material forming an ore-bed and provided with dead-blocks arranged to deflect the current from the sides of the bed or ends of its pockets, substantially as and for the pur- 3. In a separator; a series of pockets containing loose material forming an ore-bed, and
provided with dead-blocks at the bottom and dead-plates at the top of the bed, arranged to form blind-pockets, which confine the mate rial and prevent the passage of currents subva-pervious bottom, dead-blocks at itsends,
and deflectors arranged above the dead-blocks, substantially as and for the purposes specified. 5. A separator-pocket for an ore-bed, said pocket having a dead-block at each end near the-bottom, and a dead plate or flange extending around the pocketvat or near the level or top surface of the ore-bed, substantially as and for the purposes specified. 6. In an ore'separator, the combination,with an ore-bed, of a series of rods or bars for guarding the feed and discharge orifices of the separator, and a locked cover for closing the chamber over the ore-bed, substantially as and for the purposes specified.
In testimony whereof I afiix my signature in
Publications (1)
Publication Number | Publication Date |
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US347867A true US347867A (en) | 1886-08-24 |
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ID=2416935
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US347867D Expired - Lifetime US347867A (en) | Gold separator |
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US (1) | US347867A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2558639A (en) * | 1947-08-02 | 1951-06-26 | Walter R J Woock | Mineral separator |
US2561396A (en) * | 1946-10-09 | 1951-07-24 | Standard Oil Dev Co | Segregation of solid particles |
US2678131A (en) * | 1950-07-17 | 1954-05-11 | Robert F Dore | Dry concentrator |
-
0
- US US347867D patent/US347867A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2561396A (en) * | 1946-10-09 | 1951-07-24 | Standard Oil Dev Co | Segregation of solid particles |
US2558639A (en) * | 1947-08-02 | 1951-06-26 | Walter R J Woock | Mineral separator |
US2678131A (en) * | 1950-07-17 | 1954-05-11 | Robert F Dore | Dry concentrator |
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