US2997438A - Device for reclaiming silver from photographic hypo baths - Google Patents

Device for reclaiming silver from photographic hypo baths Download PDF

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US2997438A
US2997438A US742590A US74259058A US2997438A US 2997438 A US2997438 A US 2997438A US 742590 A US742590 A US 742590A US 74259058 A US74259058 A US 74259058A US 2997438 A US2997438 A US 2997438A
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hypo
cathodes
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anodes
plates
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Clifton E James
Fedelchak Paul
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/20Electrolytic production, recovery or refining of metals by electrolysis of solutions of noble metals

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  • Another object of this invention is to-provide a device for removing silver from hypo baths, .the device being constructed on an extremely smallscale and being feasible for operation within relatively small laboratories, such as the laboratories used in developing X-r ay film in hospitals and the like.
  • i I v Another object of this invention is to provide an electrodepositing device wherein the sum of the distance betweenan anode and a cathode and the rate offlow across such distance is substantially constantthroughout the length of the cathode.
  • Another object of this invention is to provide anim-' proved electrodepositing device for use in removing silver from photographic hypo baths, the electrodepositing device being so constructed whereby access to the anode and cathode thereof is readily obtainable so that in the event of a short, the deposited silver across the short may be readily removed to eliminate the short.
  • a further object of this invention is to provide an improved dew'ce for removing silver. from photographic hypo baths by electrodepositing such silver on cathodes, the cathodes being so mounted whereby they may be readily removed to facilitate the stripping of the deposited silver therefrom.
  • FIGURE 1 is a schematic view showing the connection between the device for reclaiming silver and a photo ⁇ graphic hypo bath;
  • FIGUREZ is an enlarged vertical sectional view taken through the device which is the subject of this invention and shows the specific details of constru'ction thereof;
  • FIGURE 3 is an enlarged perspective view of theelec tro unit of the device removed from the container thereof ⁇
  • FIGURE 4 is an enlarged perspective view of the pump and circulating unit of
  • FIGURE 6 is an enlarged horizontal sectional view
  • FIGURE 7 is an enlarged fragmentary sectional vi'evii taken substantially upon the plane indicated by the "sec; tign line 7 7 of FIGURE 5 aiid shows the particular mounting in connections between the upper ends ofth, anodes; and
  • FIGURE 8 is an enlarged fragmentary sectional View taken substantially upon the plane indicated by sectiori line 8-8 of FIGURE 5 and shows the specific mounting of the upper ends of the cathodes.
  • the device 10 is connected to'a' hypo bath 12 by means. of an intake line 14 and 'a return 'line 16 whereby the. hypo solution of the hypo bath 12 may be circulatedr through the device 10 for the purpose 'of' continuously.
  • the intake line 14 is" provided with a commerciallyavailable filter 18 where by foreign matter is removed from the hypo solutiorf prior to the entry thereofinto the device 10. Also,
  • a metering valve 20 which may be ad-i justed to control the flow of the hypo into the devicd 10 to that which is the capacity of the device 10.
  • the device 10 includes a container 22 which is preferably formed of plastic, but may be formed of any suitable non-metallic material.
  • the container 22 includes a bottom wall 24 and a body 26, the body 26 being in the form of an inverted 'frusto conical member tapering from the top to the bottom and decreasing in size so as to have a minimum cross-section at the bottom;
  • Removably carried by the container 22 is an electrode unit 28.
  • Removably carried by the electrode unit 28 is' a pump and agitating unit which is referred to in general by the reference numeral 30.
  • the electrode unit 28 includes a bottom plate .32 and a top plate'34.
  • the plates 32 and ,34 are preferably formed of suitable plastic material with the plate 32 being of a smaller diameter than the plate 34.-
  • the plates 32 and 64 have diameters corresponding to the taper of the body 26 so Referring now to FIGURE 6 in particular, it
  • the plate 34 is constructed similarly to the plate 32 and has a central opening 46 which disposed concentric to the opening 36. Also, formed in the plate 34 and Opening through the outer edge thereof are slots 48 which are disposed tangential to the opening 46. The slots 48, however, are of lesser length than the slots 38.
  • the plate 34 is also provided with bores 50 therethrough which align with the openings 40.
  • the cathodes 52 are preferably formed of stainless steel.
  • the cathodes 52 terminate at the Upper ends in upwardly projecting cars 54 which extend above the plate 34.
  • Extending about the cars 54 and clampingly engaging the cars 54 is a hoop 6 which is provided with a suitable clamp 58, such as shown in'FIGURE 5.
  • the hoop 56 overlies the plate 34 and serves not only to form an electrical connection between the cathodes 5 2, but also to retain the cathodes 52 in place relative to the plates 32 and 34.
  • the ends of the cathodes 52 are coated with wax or similar material to prevent a buildup of silver in the slots 38 and 48.
  • the anodes 60 are preferably formed of carbon and while they extend through the plate 34, they term nate in the plate 32 so as to prevent an electrolysis within the sump 44.
  • the innermost ones of the anodes 60 are engaged by a hoop 62 which overlies the plate 34 and which is provided with a clamp fitting 64 so as to tightly engage the anodes 60 and form an 'electrical'connection therewith.
  • the outermost anodes 60 areelectrically connected to the innermost anodes 60 and to the hoop 62 by means of inverted lJ-shapcd connectors 66, as is best shown in FIGURE 7.
  • the electrode unit 28 may be readily disassembled. Electrical connections with the hoops 5 6 and 62 are made by means of terminals 68 and 70, as is best shown in FIGURE 3.
  • the pump and agitator unit 30 includes a small powered electric motor 72 which is connected to a supporting plate 74 by means of bolts 76.
  • the electric motor 72 is'spaced above the supporting plate 74 by means of spacers 78.
  • the supporting plate 74- has a reduced lower portion 80 which is received in the opening 46 in the plate 34 so as to center the pump and agitator unit 30.
  • the electric motor 72 includes an elongated armature shaft 84 which extends down through a housing 86 carried by the plate 74 and depending herefrom.
  • the housing 86 has formed in the extreme upper part thereof a first pump 88.
  • a s COBd pump 90 Disposed immediately below the first pump 88 is a s COBd pump 90.
  • the pump 88 is an int ke pump whereas the pump 90 is a return pump.
  • Pump 90 includes a pump chamber 92 which has an inlet opening 94 opening through the exterior of t housing 86 int h co tainer 22- I- als includes n outlet 96 to which there is connected the return line 16.
  • T p mp 88 ha mo n ed in t e p mp chamb r 92 thereof the rotor 100 of the pump, the rotor 100 being carried by the armature shaft 84.
  • the pump 88 includes a pump chamber 102 which is com unicated wi h interior of the cont i 22 by communicated with the intake line 14 by means of a passage 106.
  • a rotor 108 mounted within the chamber 102. It is to be understood that the pumps 88 and 90 are both centrifugal pumps although other. types of pumps may be used.
  • The'lower part of the armature shaft 84 is joumalled in the housing 86 by being positioned in a longitudinal bore 110 formed therein.
  • the armature shaft 84 projects below the housing 86 and is provided with an impeller 112 for the purpose of circulating the hypo solution within the container 22.
  • a suitable thrust washer V 114 is provided between the impeller 112 and the lower end of the housing 86.
  • plating occurs only during the very initial starting time of the device and after that the present device will deposit metallic silver along with impurities such as bits of Wood, thread, dirt, gelatin and the like on the cathode.
  • impurities such as bits of Wood, thread, dirt, gelatin and the like on the cathode.
  • This buildup along the leading edge of the cathode represents impurities in the solution which have received a positive electro charge and adhere to the first cathode surface they come in contact with.
  • the current density is internally controlled within the unit and the solution is agitated to a relatively high degree in order to permit a high current density without polarization.
  • the electrolytic deposition of silver without the formation of sulphide which discolors the bath 7 and renders it useless is practical only in an acid bath;
  • the maximum current density that can be used increases within certain limits, with the degree of agitation, the temperature, the silver content, the acidity and the sulphite concentration.
  • V The advantages of the agitation become more apparent means of an outlet passage 104.
  • the chamber 102 is 16 when considering the small amount of energy required plus higher current density tolerated within the system which provides the higher silver recovery rate.
  • the physical structure of the cathode and anode assembly coupled with the velocity agitation system provides many advantages not available in currently available industrial recovery units.
  • the arrangement of the cathode permits both sides ofthis electrode to receive silver thus increasing the cathode area which permits higher solution velocity and of course permits greater current density within increased tolerance in current density. This in turn allows the construction of a smaller unit for the amount of silver recovered per gallon of hypo solution and for the electrical energy required for operation.
  • the device when a photographic laboratory is being operated, the device will continuously function.
  • the quantity of the hypo being circulated through the device 10 will be a minimum so as to not vary the temperature of the hypo solution and at the same time will be suflicient to remove the silver as it is deposited into the hypo solution.
  • the arrangement suggested in FIGURE 1 is of such a nature whereby the device 10 requires no attention whatsoever. Therefore, not only does the device 10 function without requiring special attention, except for the stripping of the silver from the cathodes 52 at extended intervals, but also it serves to save both the hypo and the silver which is normally permitted to run down the drain.
  • the pump and agitator unit 30 may be readily removed so as to permit access to the electrode unit 28.
  • the deposited material causing the short may be readily scraped away and the device 10 returned to operation.
  • there is a constant rate of depositing of the silver on the cathodes so as to produce a maximum efliciency. Therefore, the operation of the device 10 requires a minimum of current and thus makes the invention economically feasible for small operations such as X-ray developing laboratories in hospitals and the like.
  • a unit for reclaiming silver from photographic hypo baths comprising a container, an electrode unit removably disposed in said container, and a hypo circulating pump means removably mounted on said electrode unit, said electrode unit comprising an upper plate, a lower plate, said plates being disposed in vertically spaced relation, a plurality of circumferentially spaced anodes extending between said plates, a plurality of circumferentially spaced cathodes extending between said plates, said cathodes and anodes being circumferentially spaced from each other and circumferentially alternately arranged, means electrically interconnecting the upper ends of the anodes and adapted to be connected to a source of electrical energy, means electrically interconnecting the upper ends of the cathodes and adapted to be connected to a source of electrical energy, said container including a tapered peripheral wall removably and wedgedly supporting said plates, each of said plates including an enlarged central opening, said circulating pump means including a support plate removably supported in the opening in the
  • said intake pump means includes a hollow chamber in said housing, said intake extending from the center of the chamber, said housing having a radial discharge passage communicating the housing with the interior of the container, and an impeller mounted within said chamber and connected to said output shaft.
  • said discharge pump means includes a hollow chamber in said housing, said housing including intake passageways communicating the center of the chamber with the interior of the container, said discharge including a radially extending passageway.
  • cathodes are in the form of thin metallic strips disposed in outwardly diverging relation to each other, said strips being disposed in a plane tangential to the central opening.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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  • Metallurgy (AREA)
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Description

g- 1961 c. E. JAMES ET AL 2,997,438
DEVICE FOR RECLAIMING SILVER FROM PHOTOGRAPHIC HYPO BATHS Filed June 17, 1958 2 Sheets-Sheet 1 l/VTAKE F/gJ RETURN Fig-2 7 72 T HE URN 73 84 78 30 /N7I4KE 46/ l /04 n? 96 9b I0 g //4 I a /60 1/2 Clifton E. James 52/ Paul Fede/chak INVENTORS r 9 k; um BY 2 Aug. 22, 1961 c, 5, JAMES ET AL 2,997,438
DEVICE FOR RECLAIMING SILVER FROM PHOTOGRAPHIC HYPO BATE-IS Filed June 17, 1958 2 Sheets-Sheet 2 Fig-3 60 62 56 7 4 Clifton E. James Paul Fade/chair I N VE N TORS United States Patent- 2,997,438 DEVICE FOR RECLAIMING SILVER FROM PHOTOGRAPHIC HYPO BATHS Clifton E. James, McLean, Va., and Paul Fedelcliak, Bedford, Mass. (both of 13D McArthur' St.,- Westover AFB, Mass.) I 7 Filed June 17, 1958, Ser. No. 742,590
4 Claims. (Cl. 204-273) This invention relates in general to a new and useful device for the regeneration of photographic; fixing baths and reclaiming the silver therefrom by an electrolytic process. v
There are many installations in daily use processing photographic sensitized materials where the exhausted fixing baths are discarded down the drain. These solutions can be regenerated by the removal of the photosensitive silver which has been dissolved from the photographic emulsions. Heretofore there has been devised devices for the purpose of removing such silver. How ever, since the amount of silver is a relatively small one and since the cost of hypo alsorelatively low, the installations heretofore provided have been too expensive as to be economically feasible. Either these devices have either required the services of a valuable employee, or they themselves have been too expensive to purchase, install and operate.
It is therefore the primary object of this invention to provide a device for regenerating exhausted fixing baths by removing photographic silver, the deviee being so constructed whereby it will constantly transfer hypo from a hypo bath to the device and remove the silver from the hypo-in a continuous operation without requiring theattendance of the operator of the laboratory. 1
.Another object of this invention is to-provide a device for removing silver from hypo baths, .the device being constructed on an extremely smallscale and being feasible for operation within relatively small laboratories, such as the laboratories used in developing X-r ay film in hospitals and the like. i I v Another object of this invention is to provide an electrodepositing device wherein the sum of the distance betweenan anode and a cathode and the rate offlow across such distance is substantially constantthroughout the length of the cathode.
Another object of this invention is to provide anim-' proved electrodepositing device for use in removing silver from photographic hypo baths, the electrodepositing device being so constructed whereby access to the anode and cathode thereof is readily obtainable so that in the event of a short, the deposited silver across the short may be readily removed to eliminate the short.
A further object of this invention is to provide an improved dew'ce for removing silver. from photographic hypo baths by electrodepositing such silver on cathodes, the cathodes being so mounted whereby they may be readily removed to facilitate the stripping of the deposited silver therefrom.
I Still a further object of this invention is to provide an improved electrodepositing device for removing silver from photographic hypo baths, the electrodepositing de vice including a single unit which functions as an inlet pump, an outlet pump and an agitator, the unit including a small electric motor requiring a minimum of current whereby the cost of operation of the electrcdepositin device is reduced to a V 4 These together with other objects and advantages which will become subsequently apparent reside in the details of construction and operation as more fully hereinafter ice panying drawings forming a part hereof, wherein like numerals refer to like parts throughout, and in which: FIGURE 1 is a schematic view showing the connection between the device for reclaiming silver and a photo{ graphic hypo bath; i FIGUREZ is an enlarged vertical sectional view taken through the device which is the subject of this invention and shows the specific details of constru'ction thereof; FIGURE 3 is an enlarged perspective view of theelec tro unit of the device removed from the container thereof} FIGURE 4 is an enlarged perspective view of the pump and circulating unit of the'device and shows the specific details thereof; 1 FIGURE 5 is an enlarged plan view of the electro unit and shows the manner in which the anodes and cathodes are retained in place and electrically connected;
FIGURE 6 is an enlarged horizontal sectional view,
- taken substantially upon the plane indicatedby the sec tion line 6-6 of FIGURE 3 and shows the relationship of theanodes with respect to the cathodes;
FIGURE 7 is an enlarged fragmentary sectional vi'evii taken substantially upon the plane indicated by the "sec; tign line 7 7 of FIGURE 5 aiid shows the particular mounting in connections between the upper ends ofth, anodes; and
FIGURE 8 is an enlarged fragmentary sectional View taken substantially upon the plane indicated by sectiori line 8-8 of FIGURE 5 and shows the specific mounting of the upper ends of the cathodes. Referring now to the drawings in detail, it"will be'seeii that there is illustrated a typical installation utilizing the device which is the subject of this invention, the device beingreferrled to in general by the reference numeral 10. The device 10 is connected to'a' hypo bath 12 by means. of an intake line 14 and 'a return 'line 16 whereby the. hypo solution of the hypo bath 12 may be circulatedr through the device 10 for the purpose 'of' continuously.
removing the silver therefrom. The intake line 14 is" provided with a commerciallyavailable filter 18 where by foreign matter is removed from the hypo solutiorf prior to the entry thereofinto the device 10. Also,
there is provided a metering valve 20 which may be ad-i justed to control the flow of the hypo into the devicd 10 to that which is the capacity of the device 10.
Referring 'now to FIGURE 1 in particular, it will be seenthat the device 10 includes a container 22 which is preferably formed of plastic, but may be formed of any suitable non-metallic material. The container 22 includes a bottom wall 24 and a body 26, the body 26 being in the form of an inverted 'frusto conical member tapering from the top to the bottom and decreasing in size so as to have a minimum cross-section at the bottom;
Removably carried by the container 22 is an electrode unit 28. Removably carried by the electrode unit 28 is' a pump and agitating unit which is referred to in general by the reference numeral 30. v
As is best illustrated in FIGURES 2 and 3, the electrode unit 28 includes a bottom plate .32 and a top plate'34. The plates 32 and ,34 are preferably formed of suitable plastic material with the plate 32 being of a smaller diameter than the plate 34.- The plates 32 and 64 have diameters corresponding to the taper of the body 26 so Referring now to FIGURE 6 in particular, it
described and claimed, reference being had to the accom 3 40 which do not extend through the entire depth of the plate 32. Further, removed fromthe periphery of the plate 32 at circumferentially spaced intervals are mat'erials to provide recesses 42. The purpose of the open ing' 36 and recesses 42 is to facilitate theffrce flow of the hypo solution past the plate 32 and down into the portion of the container' 26 below the plate 32 which forms a sump 44. I The plate 34 is constructed similarly to the plate 32 and has a central opening 46 which disposed concentric to the opening 36. Also, formed in the plate 34 and Opening through the outer edge thereof are slots 48 which are disposed tangential to the opening 46. The slots 48, however, are of lesser length than the slots 38. The plate 34 is also provided with bores 50 therethrough which align with the openings 40. Extending between the plates 32 and 34 are plate-like cathodes 52. The cathodes 52 are preferably formed of stainless steel. The cathodes 52 terminate at the Upper ends in upwardly projecting cars 54 which extend above the plate 34. Extending about the cars 54 and clampingly engaging the cars 54 is a hoop 6 which is provided with a suitable clamp 58, such as shown in'FIGURE 5. The hoop 56 overlies the plate 34 and serves not only to form an electrical connection between the cathodes 5 2, but also to retain the cathodes 52 in place relative to the plates 32 and 34. The ends of the cathodes 52 are coated with wax or similar material to prevent a buildup of silver in the slots 38 and 48.
Extending between the plates 32 and 3,4 are also anodes 60. The anodes 60 are preferably formed of carbon and while they extend through the plate 34, they term nate in the plate 32 so as to prevent an electrolysis within the sump 44.
The innermost ones of the anodes 60 are engaged by a hoop 62 which overlies the plate 34 and which is provided with a clamp fitting 64 so as to tightly engage the anodes 60 and form an 'electrical'connection therewith. The outermost anodes 60 areelectrically connected to the innermost anodes 60 and to the hoop 62 by means of inverted lJ-shapcd connectors 66, as is best shown in FIGURE 7.
From the foregoing description of the electrode unit 28', it will be readily apparent that by releasing the hoops 56 and 62, the electrode unit 28 may be readily disassembled. Electrical connections with the hoops 5 6 and 62 are made by means of terminals 68 and 70, as is best shown in FIGURE 3.
Referring now to FIGURES 2 and 4 in particular, it will be seen that the pump and agitator unit 30 includes a small powered electric motor 72 which is connected to a supporting plate 74 by means of bolts 76. The electric motor 72 is'spaced above the supporting plate 74 by means of spacers 78. The supporting plate 74- has a reduced lower portion 80 which is received in the opening 46 in the plate 34 so as to center the pump and agitator unit 30.
The electric motor 72 includes an elongated armature shaft 84 which extends down through a housing 86 carried by the plate 74 and depending herefrom. The housing 86 has formed in the extreme upper part thereof a first pump 88. Disposed immediately below the first pump 88 is a s COBd pump 90. The pump 88 is an int ke pump whereas the pump 90 is a return pump.
Pump 90 includes a pump chamber 92 which has an inlet opening 94 opening through the exterior of t housing 86 int h co tainer 22- I- als includes n outlet 96 to which there is connected the return line 16. T p mp 88 ha mo n ed in t e p mp chamb r 92 thereof the rotor 100 of the pump, the rotor 100 being carried by the armature shaft 84.
The pump 88 includes a pump chamber 102 which is com unicated wi h interior of the cont i 22 by communicated with the intake line 14 by means of a passage 106. Mounted within the chamber 102 is a rotor 108 carried by the armature shaft 84. It is to be understood that the pumps 88 and 90 are both centrifugal pumps although other. types of pumps may be used.
The'lower part of the armature shaft 84 is joumalled in the housing 86 by being positioned in a longitudinal bore 110 formed therein. The armature shaft 84 proiects below the housing 86 and is provided with an impeller 112 for the purpose of circulating the hypo solution within the container 22. A suitable thrust washer V 114 is provided between the impeller 112 and the lower end of the housing 86.
' Referring once again to FIGURE 6 in particular, it will be seen that as the impeller 112 rotates, the hypo solution within the container 22 will be circulated and thrown outwardly tangentially between the cathodes. 52. As the hypo solution is circulated between the cathodes 52 andthe anodes 69, silver carried by the hypo solution. will be deposited on the cathodes 52. It will be readily apparent from the arrangement of the cathodes 52 and the anodes 60 in FIGURE 6 that as the hypo solution moves outwardly, the velocity of flow will decrease due to the divergence of the cathodes 52 outwardly thereby increasing the spacing between the cathodes 52 and the anodes 60.
It is pointed out that plating occurs only during the very initial starting time of the device and after that the present device will deposit metallic silver along with impurities such as bits of Wood, thread, dirt, gelatin and the like on the cathode. This buildup along the leading edge of the cathode represents impurities in the solution which have received a positive electro charge and adhere to the first cathode surface they come in contact with.
It is known that in the electrolytic separation of the metal from the aqueous solution of a simple salt, the metal ions travel towards the cathode where it is discharged and becomes an atom of the metal. The acid ion travels to the anode to which it attaches or it libcrates oxygen by reacting with water. In the electrolysis of the complex salt sodium argentothiosulphate, sodium ions migrate to the cathode and argentothiosulphate ions move towards the anode. The sodium atoms formed at the cathode react with neighbouring ions in solution, including the argentothiosulphate ions. When there are sufiicient argentothiosulphate ions, the sodium atoms react with these thus liberating silver.
Thus, it will be seen that metallic silver is produced by a secondary reaction on ions which are tending to move away from the electrode on which the metal is deposited. In order to ensure a suflicient concentration of argentothiosulphate ions at the cathode, it is necessary to either stir or agitate the solution quite vigorously so that a high current density may be used or to limit the current density to a few milliamperes per square decimeter of electrode surface. The second mentioned procedure would cause the use of a very large electrode surface in order to achieve an industrially practical rate of recovery. Therefore, the present invention incorporates the vigorous agitation of the solution in order to ensure a sutficient concentration of argentothiosulphate ions at the cathode.
In view of the foregoing, it will be understood that the current density is internally controlled within the unit and the solution is agitated to a relatively high degree in order to permit a high current density without polarization. Further, the electrolytic deposition of silver without the formation of sulphide which discolors the bath 7 and renders it useless is practical only in an acid bath;
The maximum current density that can be used, increases within certain limits, with the degree of agitation, the temperature, the silver content, the acidity and the sulphite concentration. V The advantages of the agitation become more apparent means of an outlet passage 104. The chamber 102 is 16 when considering the small amount of energy required plus higher current density tolerated within the system which provides the higher silver recovery rate. The physical structure of the cathode and anode assembly coupled with the velocity agitation system provides many advantages not available in currently available industrial recovery units. The arrangement of the cathode permits both sides ofthis electrode to receive silver thus increasing the cathode area which permits higher solution velocity and of course permits greater current density within increased tolerance in current density. This in turn allows the construction of a smaller unit for the amount of silver recovered per gallon of hypo solution and for the electrical energy required for operation.
It is the intent of this invention that when a photographic laboratory is being operated, the device will continuously function. The quantity of the hypo being circulated through the device 10 will be a minimum so as to not vary the temperature of the hypo solution and at the same time will be suflicient to remove the silver as it is deposited into the hypo solution. By so doing, not only will the life of the hypo solution be extended, thus resulting in the saving of the cost of hypo, but also valuable silver will be removed from the hypo solution, which silver may be reclaimed. The arrangement suggested in FIGURE 1 is of such a nature whereby the device 10 requires no attention whatsoever. Therefore, not only does the device 10 function without requiring special attention, except for the stripping of the silver from the cathodes 52 at extended intervals, but also it serves to save both the hypo and the silver which is normally permitted to run down the drain.
Because of the particular construction of the device 10, the pump and agitator unit 30 may be readily removed so as to permit access to the electrode unit 28. Thus in the event there should be any minor shorting between the anodes and cathodes, the deposited material causing the short may be readily scraped away and the device 10 returned to operation. Further, because of the particular manner in which the anodes and cathodes are related, there is a constant rate of depositing of the silver on the cathodes so as to produce a maximum efliciency. Therefore, the operation of the device 10 requires a minimum of current and thus makes the invention economically feasible for small operations such as X-ray developing laboratories in hospitals and the like.
From the foregoing, the construction and operation of the device will be readily understood and further explanation is believed to be unnecessary. However, since numerous modifications and changes will readily occur to those skilled in the art, it is not desired to limit the invention to the exact construction shown and described, and accordingly all suitable modifications and equivalents may be resorted to, falling within the scope of the invention as claimed.
What is claimed as new is as follows:
1. A unit for reclaiming silver from photographic hypo baths comprising a container, an electrode unit removably disposed in said container, and a hypo circulating pump means removably mounted on said electrode unit, said electrode unit comprising an upper plate, a lower plate, said plates being disposed in vertically spaced relation, a plurality of circumferentially spaced anodes extending between said plates, a plurality of circumferentially spaced cathodes extending between said plates, said cathodes and anodes being circumferentially spaced from each other and circumferentially alternately arranged, means electrically interconnecting the upper ends of the anodes and adapted to be connected to a source of electrical energy, means electrically interconnecting the upper ends of the cathodes and adapted to be connected to a source of electrical energy, said container including a tapered peripheral wall removably and wedgedly supporting said plates, each of said plates including an enlarged central opening, said circulating pump means including a support plate removably supported in the opening in the upper plate, a motor carried by said support plate, a depending housing carried by said support plate, said motor including an output shaft extending downwardly through said support plate, said housing having a bore extending therethrough rotatably receiving the output shaft, said output shaft terminating intermediate the upper and lower plates, an impeller mounted on the terminal end of said output shaft, said anodes and cathodes being disposed radially outwardly of the im peller whereby the impeller will circulate hypo within the container and move hypo past the anodes and cathodes when the motor is energized, said circulating pump means also including intake pump means mounted in the housing and driven from said shaft, said intake pump means having an intake communicated with a supply of hypo and a discharge communicated with the interior of the container, and a discharge pump means mounted in the housing and driven from said shaft, said discharge pump means including an intake communicated with the interior of the container and a discharge communicated with a supply of hypo for circulating hypo through said unit.
2. The combination of claim 1 wherein said intake pump means includes a hollow chamber in said housing, said intake extending from the center of the chamber, said housing having a radial discharge passage communicating the housing with the interior of the container, and an impeller mounted within said chamber and connected to said output shaft.
3. The combination of claim 1 wherein said discharge pump means includes a hollow chamber in said housing, said housing including intake passageways communicating the center of the chamber with the interior of the container, said discharge including a radially extending passageway. t
4. The combination of claim 1 wherein said cathodes are in the form of thin metallic strips disposed in outwardly diverging relation to each other, said strips being disposed in a plane tangential to the central opening.
References Cited in the file of this patent UNITED STATES PATENTS 775,597 Cassel Nov. 22, 1904 1,535,400 Crowell Apr. 28, 1925 2,011,204 Spang Aug. 13, 1935 2,158,410 Doran May 16, 1939 2,791,555 Duisenberg May 7, 1957 FOREIGN PATENTS 491,453 Canada Mar. 24, 1953

Claims (1)

1. A UNIT FOR RECLAIMING SILVER FROM PHOTOGRAPHIC HYPO BATHS COMPRISING A CONTAINER, AN ELECTRODE UNIT REMOVABLY DISPOSED IN SAID CONTAINER, AND A HYPO CIRCULATING PUMP MEANS REMOVABLY MOUNTED ON SAID ELECTRODE UNIT, SAID ELECTRODE UNIT COMPRISING AN UPPER PLATE, A LOWER PLATE, SAID PLATES BEING DISPOSED IN VERTICALLY SPACED RELATION, A PLURALITY OF CIRCUMFERENTIALLY SPACED ANODES EXTENDING BETWEEN SAID PLATES, A PLURALITY OF CIRCUMFERENTIALLY SPACED CATHODES EXTENDING BETWEEN SAID PLATES, SAID CATHODES AND ANODES BEING CIRCUMFERENTIALLY SPACED FROM EACH OTHER AND CIRCUMFERENTIALLY ALTERNATELY ARRANGED, MEANS ELECTRICALLY INTERCONNECTING THE UPPER ENDS OF THE ANODES AND ADAPTED TO BE CONNECTED TO A SOURCE OF ELECTRICAL ENERGY, MEANS ELECTRICALLY INTERCONNECTING THE UPPER ENDS OF THE CATHODES AND ADAPTED TO BE CONNECTED TO A SOURCE OF ELECTRICAL ENERGY, SAID CONTAINER INCLUDING A TAPERED PERIPHERAL WALL REMOVABLY AND WEDGEDLY SUPPORTING SAID PLATES, EACH OF SAID PLATES INCLUDING AN ENLARGED CENTRAL OPENING, SAID CIRCULATING PUMP MEANS INCLUDING A SUPPORT PLATE REMOVABLY SUPPORTED IN THE OPENING IN THE UPPER PLATE, A MOTOR CARRIED BY SAID SUPPORT PLATE, A DEPENDING HOUSING CARRIED BY SAID SUPPORT PLATE, SAID MOTOR INCLUDING AN OUTPUT SHAFT EXTENDING DOWNWARDLY THROUGH SAID SUPPORT PLATE, SAID HOUSING HAVING A BORE EXTENDING THERETHROUGH ROTATABLY RECEIVING THE OUTPUT SHAFT, SAID OUTPUT SHAFT TERMINATING INTERMEDIATE THE UPPER AND LOWER PLATES, AN IMPELLER MOUNTED ON THE TERMINAL END OF SAID OUTPUT SHAFT, SAID ANODES AND CATHODES BEING DISPOSED RADIALLY OUTWARDLY OF THE IMPELLER WHEREBY THE IMPELLER WILL CIRCULATE HYPO WITHIN THE CONTAINER AND MOVE HYPO PAST THE ANODES AND CATHODES WHEN THE MOTOR IS ENERGIZED, SAID CIRCULATING PUMP MEANS ALSO INCLUDING INTAKE PUMP MEANS MOUNTED IN THE HOUSING AND DRIVEN FROM SAID SHAFT, SAID INTAKE PUMP MEANS HAVING AN INTAKE COMMUNICATED WITH A SUPPLY OF HYPO AND A DISCHARGE COMMUNICATED WITH THE INTERIOR OF THE CONTAINER, AND A DISCHARGE PUMP MEANS MOUNTED IN THE HOUSING AND DRIVEN FROM SAID SHAFT, SAID DISCHARGE PUMP MEANS INCLUDING AN INTAKE COMMUNICATED WITH THE INTERIOR OF THE CONTAINER AND A DISCHARGE COMMUNICATED WITH A SUPPLY OF HYPO FOR CIRCULATING HYPO THROUGH SAID UNIT.
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3271282A (en) * 1963-06-18 1966-09-06 Photo Engravers Res Inc Process for etching photoengraving copper
US3342718A (en) * 1964-01-21 1967-09-19 William M Adams Apparatus for the recovery of silver from used photographic fixing solutions by electrolysis
US3397135A (en) * 1964-09-21 1968-08-13 Julius L Englesberg Integral pump and filter assembly including electrode means
US4026784A (en) * 1975-11-10 1977-05-31 Rivers James R Metal recovery unit
US4054503A (en) * 1976-10-14 1977-10-18 Ag-Met, Inc. Portable metal recovery apparatus
US4069127A (en) * 1976-02-04 1978-01-17 Ecological Systems, Inc. Method and apparatus for recovery of metal from liquid
US4302317A (en) * 1976-04-05 1981-11-24 Mock Karl J Means for recovering a precious metal from an electrolyte solution containing ions of said metal
US4639302A (en) * 1982-12-10 1987-01-27 Dextec Metallurgical Pty. Ltd. Electrolytic cell for recovery of metals from metal bearing materials
US4840717A (en) * 1988-08-24 1989-06-20 Dzodin Milton A Silver recovery cell
US5282934A (en) * 1992-02-14 1994-02-01 Academy Corporation Metal recovery by batch electroplating with directed circulation

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US775597A (en) * 1903-05-22 1904-11-22 Henry R Cassel Process of extracting gold from ores.
US1535400A (en) * 1922-01-11 1925-04-28 Crowell Rufus Method and apparatus for forming tubing electrolytically
US2011204A (en) * 1934-04-23 1935-08-13 Joseph P Spang Apparatus for aging liquor, wine, and other beverages while stored in a barrel
US2158410A (en) * 1935-06-15 1939-05-16 Internat Cinema Inc Method and apparatus for the recovery of metal from a liquid
CA491453A (en) * 1953-03-24 Leverenz Wilhelm Process and equipment for electrolytical regeneration of exhausted photographical fixative baths
US2791555A (en) * 1955-04-11 1957-05-07 Charles E Duisenberg Apparatus for rejuvenating and prolonging the life of hypo solutions

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA491453A (en) * 1953-03-24 Leverenz Wilhelm Process and equipment for electrolytical regeneration of exhausted photographical fixative baths
US775597A (en) * 1903-05-22 1904-11-22 Henry R Cassel Process of extracting gold from ores.
US1535400A (en) * 1922-01-11 1925-04-28 Crowell Rufus Method and apparatus for forming tubing electrolytically
US2011204A (en) * 1934-04-23 1935-08-13 Joseph P Spang Apparatus for aging liquor, wine, and other beverages while stored in a barrel
US2158410A (en) * 1935-06-15 1939-05-16 Internat Cinema Inc Method and apparatus for the recovery of metal from a liquid
US2791555A (en) * 1955-04-11 1957-05-07 Charles E Duisenberg Apparatus for rejuvenating and prolonging the life of hypo solutions

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3271282A (en) * 1963-06-18 1966-09-06 Photo Engravers Res Inc Process for etching photoengraving copper
US3342718A (en) * 1964-01-21 1967-09-19 William M Adams Apparatus for the recovery of silver from used photographic fixing solutions by electrolysis
US3397135A (en) * 1964-09-21 1968-08-13 Julius L Englesberg Integral pump and filter assembly including electrode means
US4026784A (en) * 1975-11-10 1977-05-31 Rivers James R Metal recovery unit
US4069127A (en) * 1976-02-04 1978-01-17 Ecological Systems, Inc. Method and apparatus for recovery of metal from liquid
US4302317A (en) * 1976-04-05 1981-11-24 Mock Karl J Means for recovering a precious metal from an electrolyte solution containing ions of said metal
US4054503A (en) * 1976-10-14 1977-10-18 Ag-Met, Inc. Portable metal recovery apparatus
US4639302A (en) * 1982-12-10 1987-01-27 Dextec Metallurgical Pty. Ltd. Electrolytic cell for recovery of metals from metal bearing materials
US4840717A (en) * 1988-08-24 1989-06-20 Dzodin Milton A Silver recovery cell
US5282934A (en) * 1992-02-14 1994-02-01 Academy Corporation Metal recovery by batch electroplating with directed circulation

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