US578953A - Tank for treating alloys - Google Patents
Tank for treating alloys Download PDFInfo
- Publication number
- US578953A US578953A US578953DA US578953A US 578953 A US578953 A US 578953A US 578953D A US578953D A US 578953DA US 578953 A US578953 A US 578953A
- Authority
- US
- United States
- Prior art keywords
- tank
- cells
- anode
- carriages
- alloys
- 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
- 229910045601 alloy Inorganic materials 0.000 title description 9
- 239000000956 alloy Substances 0.000 title description 9
- 239000004020 conductor Substances 0.000 description 10
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 4
- 238000005868 electrolysis reaction Methods 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
- 229910052709 silver Inorganic materials 0.000 description 3
- 239000004332 silver Substances 0.000 description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 230000001413 cellular effect Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229910052949 galena Inorganic materials 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000003405 preventing effect Effects 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/10—Agitating of electrolytes; Moving of racks
Definitions
- My invention relates to improvements in apparatus for separating or extracting metals by electrolysis, its object being to insert the receptacles containing the alloy or metalliferous body into the tanks for electrolysis in such a manner that they can be readily moved within the liquid in the tank in a horizontal direction, that they can be readily inserted and lifted out, and to make them adjustable in a vertical direction for the purpose of preven ting short-circuiting.
- Figure 1 is a longitudinal elevation, partly in section of an apparatus embodying my invention, part being shown broken away.
- Fig. 2 is a plan view of Fig. 1.
- Fig. 3 is a vertical section of the same on the line 3 3
- Fig. Fig. i is a side elevation, on a smaller scale, of the apparatus.
- Fig. 5 is a plan view of Fig. a.
- Fig. 6 is a perspective view of a modified form for the anode-conductor.
- Fig. 7 is aperspective view of a removable tray.
- the letter A designates a tank for containing an electrolytic bath.
- the tank is made in the usual manner, by preference oblong, but it may also he made annular.
- the bottom of the tank may be kept warm by heating-pipes, such as the steampipes P, (shown in the drawings,) placed into the space beneath the bottom.
- cells or receptacles for alloys or met alliferous bodies I) to be suspended within the bath are by preference made square or oblong, of wood, metal, or other suit able material.
- the bottom of the cells as shown in the drawings, has perforations p and is covered by a filtering-cloth 0. (Shown partly turned up in Fig. 2.)
- the bottom may, however, be formed and rendered permeable in any suitable manner and the cells may be Serial No. 596,826. (No model.)
- a cellular conductor in, such as shown in Fig. 6.
- the cells or receptacles B are adjustably supported upon carriages consisting, in the example shown, of side pieces D, transverse pieces d, brackets e, and wheels f. Adjusting-screws s, mounted in top flanges of the cells and resting upon the cross-pieces (1, form the means for vertically adjusting the cells upon the carriages respectively within the bath.
- R are rails upon which the carriages run, and one or both of which may be properly insulated and serve as electrical conductors.
- the carriages may, however, be constructed in any other suitable manner which will permit horizontal motion.
- 9 g are eyebolts for lifting out and inserting the cells by hoisting apparatus.
- the apparatus is to be used for electrolytic purposes, I use a conductor 7t for the positive current, said conductor being, by preference, cast of the alloy to be treated and connected to the wire iby a suitable bindingscrew.
- the conductor may, however, be cast in any other form-such, for instance, as the cellular form shown in Fig. 6and it may be made of conducting material not soluble in the liquid, so as to give a large surface of contact for fine material.
- the current is supplied to the anode-conductor K from the insulated rail R, through a bar qand wire t', the bar q having a shoe 1', adapted to form a sliding contact with the rail and held by bolts 2', passing through oblong holes.
- the current may, however, be supplied in any other well-known manner from a separate conductor with a sliding contact or with direct connection to the conductor K by means of an elastic wire permitting the motion of the carriage.
- the cathode 0 may be formed of one or more pieces fastened to the bottom of the tank A, each of the pieces being connected to the source of electricity. It may, however, be made of several shallow removable trays, such as the metallic tray 0 shown in Fig. 7, which is placed upon the cathode O and may be lifted out by the use of forked hooks when the anode-cell is pushed aside.
- the receptacles or cells can be readily moved within the liquid in a horizontal direction. They are readily inserted and also removed and adjusted in a vertical direction, so as to prevent shortcircuiting between the anodes and cathodes.
- the apparatus may be used for leaching metalliferous bodies and for electrolysis or forboth combined.
- the cellsB maybe moved by hand or they may be connected by links L and moved by apparatus such as the rod H and arm G, operated from pullcyE through a crank and link F, Fig. 4.
- By moving the cells back and forth stirring and mixing of the liquid is effected, gasbubbles are driven off, and, in fact, the same effect is produced as by forced circulation of the liquid in leach ing or electrolytic tanks.
- Gold, silver, lead, tin, zinc, and other metals which are mostly deposited by the electric current in a finely-divided spongy or crystalline form, may easily be removed from the tank without interrupting the process.
- the anode-cells are simply rolled apart and the metal removed from the intermediate space by a shovel, or when removable cathode-trays are used they are lifted out and emptied.
- the anodecells B When the apparatus is used for the extraction of gold or other metals from comparatively poor ores or for stripping work, such as removing tin from tin-scrap, the anodecells B must be made extra strong, the same also for the parting of alloys, such as lead bullion, or for the reduction of galena when heavy weights of metals or ore must be charged and worked in a short time.
- the apparatus is especially applicable.
- the anode-cells in this case should be lined with filtering-cloth, upon which the gold, platinum, &c., remain in the form of a fine slime, while the silver is deposited upon the cathode in a granular or crystalline form and shoveled out at certain intervals through the open spaces formed between any two cells.
- an electrolytic tank anode cells with permeable bottoms
- carriages constructed to support said anode-cells when immersed into the tank and adapted to be moved horizontally; means for vertically adjusting the anode-cells upon the carriages; one or more cathodes at the bottom of the tank; and suitable electric connections for the electrodes, substantially as and for the purpose specified.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Description
2 Sheets-Sheet 1.
Patented Mar. 16,1897.
F. A. THUM.
TANK FOR TREATING ALLOYS, &c.
(No Model.)
[V INVENTOR e/mdmo /Zm I BY A ATTORNEY WITNESSES: W m
WWW
(No Model.) 2 Sheets-Sheet 2' F. A. THUM.
TANK FOR TREATING ALLOYS, &c.
No, 578.953 Patented Mar. 16,1897.
N INVENTOR'. tfiuwa Z.
WITNESSES:
BY A WM ATTORNEY LMAV ilNrTnn STATES PATENT Qrrrcn.
FREDERIO A. THUII, OF NElVAR-K, NEIV JERSEY.
TANK FOR TREATlNG ALLOYS, 85C.
SPECIFICATION forming part of Letters Patent No. 578,953, dated March 16, 1897'.
Application filed June 26,1896.
To all 1.0710777, it Hwy concern:
Be it known that I, FREDERIC A. THUM, a citizen of the German Empire, and a resident of Newark, in the county of Essex and State of New Jersey, have invented certain new and useful Improvements in Tanks for Treating Alloys or Metalliferous Matter, of which the following is a specification.
My invention relates to improvements in apparatus for separating or extracting metals by electrolysis, its object being to insert the receptacles containing the alloy or metalliferous body into the tanks for electrolysis in such a manner that they can be readily moved within the liquid in the tank in a horizontal direction, that they can be readily inserted and lifted out, and to make them adjustable in a vertical direction for the purpose of preven ting short-circuiting.
The nature of in y invention will be best understood by reference to the annexed drawings, in which Figure 1 is a longitudinal elevation, partly in section of an apparatus embodying my invention, part being shown broken away. Fig. 2 is a plan view of Fig. 1. Fig. 3 is a vertical section of the same on the line 3 3, Fig. Fig. i is a side elevation, on a smaller scale, of the apparatus. Fig. 5 is a plan view of Fig. a. Fig. 6 is a perspective view of a modified form for the anode-conductor. Fig. 7 is aperspective view of a removable tray.
Similar letters refer to similar parts throughout the several views.
In the drawings the letter A designates a tank for containing an electrolytic bath. The tank is made in the usual manner, by preference oblong, but it may also he made annular. The bottom of the tank may be kept warm by heating-pipes, such as the steampipes P, (shown in the drawings,) placed into the space beneath the bottom.
15 are cells or receptacles for alloys or met alliferous bodies I) to be suspended within the bath. These cells are by preference made square or oblong, of wood, metal, or other suit able material. The bottom of the cells, as shown in the drawings, has perforations p and is covered by a filtering-cloth 0. (Shown partly turned up in Fig. 2.) The bottom may, however, be formed and rendered permeable in any suitable manner and the cells may be Serial No. 596,826. (No model.)
subdivided, for instance, by inserting a cellular conductor in, such as shown in Fig. 6.
The cells or receptacles B are adjustably supported upon carriages consisting, in the example shown, of side pieces D, transverse pieces d, brackets e, and wheels f. Adjusting-screws s, mounted in top flanges of the cells and resting upon the cross-pieces (1, form the means for vertically adjusting the cells upon the carriages respectively within the bath. R are rails upon which the carriages run, and one or both of which may be properly insulated and serve as electrical conductors. The carriages may, however, be constructed in any other suitable manner which will permit horizontal motion. 9 g are eyebolts for lifting out and inserting the cells by hoisting apparatus.
XVhen the apparatus is to be used for electrolytic purposes, I use a conductor 7t for the positive current, said conductor being, by preference, cast of the alloy to be treated and connected to the wire iby a suitable bindingscrew. The conductor may, however, be cast in any other form-such, for instance, as the cellular form shown in Fig. 6and it may be made of conducting material not soluble in the liquid, so as to give a large surface of contact for fine material. In the example shown the current is supplied to the anode-conductor K from the insulated rail R, through a bar qand wire t', the bar q having a shoe 1', adapted to form a sliding contact with the rail and held by bolts 2', passing through oblong holes. The current may, however, be supplied in any other well-known manner from a separate conductor with a sliding contact or with direct connection to the conductor K by means of an elastic wire permitting the motion of the carriage.
(I designates a cathode to which the negative current is carried from wire m through bar Z. The cathode 0 maybe formed of one or more pieces fastened to the bottom of the tank A, each of the pieces being connected to the source of electricity. It may, however, be made of several shallow removable trays, such as the metallic tray 0 shown in Fig. 7, which is placed upon the cathode O and may be lifted out by the use of forked hooks when the anode-cell is pushed aside.
By the arrangement shown the receptacles or cells can be readily moved within the liquid in a horizontal direction. They are readily inserted and also removed and adjusted in a vertical direction, so as to prevent shortcircuiting between the anodes and cathodes. The apparatus may be used for leaching metalliferous bodies and for electrolysis or forboth combined. The cellsB maybe moved by hand or they may be connected by links L and moved by apparatus such as the rod H and arm G, operated from pullcyE through a crank and link F, Fig. 4. By moving the cells back and forth stirring and mixing of the liquid is effected, gasbubbles are driven off, and, in fact, the same effect is produced as by forced circulation of the liquid in leach ing or electrolytic tanks. By disconnecting any number of the carriages, so as to leave them at the left-hand end of the tank A, an open space will be left through which deposits may be shoveled or raked out from the oathode below. In Fig. 5 the carriages are shown at the extreme right-hand position, and when stopped in this position room is left at the left-hand end for shoveling out deposits from the cathode.
Gold, silver, lead, tin, zinc, and other metals, which are mostly deposited by the electric current in a finely-divided spongy or crystalline form, may easily be removed from the tank without interrupting the process. For this purpose the anode-cells are simply rolled apart and the metal removed from the intermediate space by a shovel, or when removable cathode-trays are used they are lifted out and emptied.
When the apparatus is used for the extraction of gold or other metals from comparatively poor ores or for stripping work, such as removing tin from tin-scrap, the anodecells B must be made extra strong, the same also for the parting of alloys, such as lead bullion, or for the reduction of galena when heavy weights of metals or ore must be charged and worked in a short time.
For refiningauriferous silver the apparatus is especially applicable. The anode-cells in this case should be lined with filtering-cloth, upon which the gold, platinum, &c., remain in the form of a fine slime, while the silver is deposited upon the cathode in a granular or crystalline form and shoveled out at certain intervals through the open spaces formed between any two cells.
What I claim as new is 1. In an apparatus of the character specified, the combination of an electrolytic tank; anode cells with permeable bottoms; carriages constructed to support said anode-cells when immersed into the tank and adapted to be moved horizontally; one or more cathodes placed upon the bottom of the tank, and suitable electric connections for the electrodes, substantially as and for the purpose specified.
2. In an apparatus of the character specified, the combination of an electrolytic tank; anode cells with permeable bottoms; carriages constructed to support said anode-cells when immersed into the tank and adapted to be moved horizontally; means for vertically adjusting the anode-cells upon the carriages; one or more cathodes at the bottom of the tank; and suitable electric connections for the electrodes, substantially as and for the purpose specified.
In testimony that I claim the foregoing as my invention 1 have signed my name, in presence of two witnesses, this 19th day of June, 1896.
FREDERIG A. THUM.
Witnesses:
FREDERIO XV. \VARD, MIRIAM LUKE.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US578953A true US578953A (en) | 1897-03-16 |
Family
ID=2647639
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US578953D Expired - Lifetime US578953A (en) | Tank for treating alloys |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US578953A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2865832A (en) * | 1953-06-10 | 1958-12-23 | Edgar C Pitzer | Electrolytic dissolution of stainless steel |
-
0
- US US578953D patent/US578953A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2865832A (en) * | 1953-06-10 | 1958-12-23 | Edgar C Pitzer | Electrolytic dissolution of stainless steel |
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