GB2078782A - Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom - Google Patents

Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom Download PDF

Info

Publication number
GB2078782A
GB2078782A GB8020182A GB8020182A GB2078782A GB 2078782 A GB2078782 A GB 2078782A GB 8020182 A GB8020182 A GB 8020182A GB 8020182 A GB8020182 A GB 8020182A GB 2078782 A GB2078782 A GB 2078782A
Authority
GB
United Kingdom
Prior art keywords
cathode
silver
solution
plate
recovery
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.)
Withdrawn
Application number
GB8020182A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB8020182A priority Critical patent/GB2078782A/en
Publication of GB2078782A publication Critical patent/GB2078782A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/007Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells comprising at least a movable electrode
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The top edge of a cathode plate 14 is fixed to a horizontal shaft just above the solution 12 in a container of used fix solution and the plate is caused to oscillate about the shaft centre in the manner of a pendulum, causing a pressure difference to occur in the body of the solution between one side of the plate and the other. As the liquid flows around the edges of the plate to correct this difference at each oscillation, vortices are induced in the liquid which vigorously agitate the surface of the plate. <IMAGE>

Description

SPECIFICATION Silver Recovery Agitation System In the photographic process only a part of the silver present in the emulsion coating is used to form the permanent image. That part which is not thus used is dissolved out into the fix or/and bleach solutions as silver ions, depending on whether black and white or colour film or paper is being processed. The presence of these silver ions in increasing quantity reduces the efficiency of the fixing process and, if disposed of in drainage systems, is a severe pollutant and is a waste of a valuable commodity. For this reason silver recovery devices are used to remove these siver ions from solution.
Two types of recovery are common, one using ion exchange technique, the other using electrolysis.
This patent is concerned with that type of recovery using electrolysis. Commonly the electrolytic recovery system consists of a container to hold the electrically conducting fix solution, an anode of a corrosion resistant conductor such as carbon and a cathode often of stainless steel, together with an external D.C.
voltage supply. When the D.C. current is applied across the anode and cathode silver ions migrate to the cathode and are plated on to it as metallic silver.
It is advantageous to agitate the solution during this process by movement of the anode or cathode or a separate pump or agitator or a combination of these. This is often achieved by a continuously rotating cathode. This prevents the formation of silver sulphide in the fix solution which may occur if the solution adjacent to the cathode becomes denuded of silver ions, as this spoils the fix solution for re-use and contaminates the silver plate. With agitation a higher recovery current may be used without sulphiding. Once a heavy plate is collected the cathode must be removed from the container and the silver broken from it.
Many of the present cathode constructions used to agitate the liquid are complex and not easy to remove from the apparatus.
This invention is concerned with means of agitating the fix container by use of a flat cathode plate which can subsequently be removed easily for breaking off the silver.
Reference to the drawings gives a better understanding of the invention.
Fig. 1 is a side section view of the silver recovery container.
Fig. 2 is a top view of the same container.
Fig. 3 shows a section through a similar system with more than one cathode plate.
In Fig. 1: No. 11 is the solution container.
No. 12 is the fix or bleach fix solution contained in it.
No. 13 is the anode or anodes which may be fitted both sides of the cathode No. 14.
In Fig. 2: No. 7 is a gap at least at one end of the cathode between the cathode and the side wall of the tank.
In use the tank may be filled with solution to any level. The cathode is made to oscillate in directions 15, 16 pivoting at 17 in the manner of a pendulum. Movement in the direction 15 causes an increase in solution pressure on that side causing a flow of liquid through gap 7 and formation of a vortex on side 16 with subsequent vigorous agitation of the whole body of solution and most particularly adjacent to the cathode surface. On the return swing the reverse action occurs.
The pivot 17 is generally positioned above the solution level and the cathode plate can be detached at this point by releasing wing nut 18.
Insulating blocks are fitted at position 19 to prevent any possibility of the anode and cathode touching.
Fig. 3 shows a similar tank with two cathode plates.
Speeds of oscillation up to 60 per minute have been used.
When the plate moves in direction 15 vortices occur in the liquid at 19 and vice versa when moving in the opposite direction. The liquid flow causes the vortices to move towards the centre of the plate.
Claims
1. A means of agitating the liquid in a silver recovery system by which the cathode is caused to oscillate about a fixed horizontal axis in the manner of a pendulum, causing the liquid pressure to increase on one side of the plate and to decrease on the opposite side of the plate with subsequent flow of liquid from one side of the plate to the other causing vortices to agitate the cathode surface.
2. A silver recovery agitation system as in Claim 1 with anode and cathode connections reversed.
3. A silver recovery agitation system as in Claim 1 but with two or more oscillating plates.
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (3)

**WARNING** start of CLMS field may overlap end of DESC **. SPECIFICATION Silver Recovery Agitation System In the photographic process only a part of the silver present in the emulsion coating is used to form the permanent image. That part which is not thus used is dissolved out into the fix or/and bleach solutions as silver ions, depending on whether black and white or colour film or paper is being processed. The presence of these silver ions in increasing quantity reduces the efficiency of the fixing process and, if disposed of in drainage systems, is a severe pollutant and is a waste of a valuable commodity. For this reason silver recovery devices are used to remove these siver ions from solution. Two types of recovery are common, one using ion exchange technique, the other using electrolysis. This patent is concerned with that type of recovery using electrolysis. Commonly the electrolytic recovery system consists of a container to hold the electrically conducting fix solution, an anode of a corrosion resistant conductor such as carbon and a cathode often of stainless steel, together with an external D.C. voltage supply. When the D.C. current is applied across the anode and cathode silver ions migrate to the cathode and are plated on to it as metallic silver. It is advantageous to agitate the solution during this process by movement of the anode or cathode or a separate pump or agitator or a combination of these. This is often achieved by a continuously rotating cathode. This prevents the formation of silver sulphide in the fix solution which may occur if the solution adjacent to the cathode becomes denuded of silver ions, as this spoils the fix solution for re-use and contaminates the silver plate. With agitation a higher recovery current may be used without sulphiding. Once a heavy plate is collected the cathode must be removed from the container and the silver broken from it. Many of the present cathode constructions used to agitate the liquid are complex and not easy to remove from the apparatus. This invention is concerned with means of agitating the fix container by use of a flat cathode plate which can subsequently be removed easily for breaking off the silver. Reference to the drawings gives a better understanding of the invention. Fig. 1 is a side section view of the silver recovery container. Fig. 2 is a top view of the same container. Fig. 3 shows a section through a similar system with more than one cathode plate. In Fig. 1: No. 11 is the solution container. No. 12 is the fix or bleach fix solution contained in it. No. 13 is the anode or anodes which may be fitted both sides of the cathode No. 14. In Fig. 2: No. 7 is a gap at least at one end of the cathode between the cathode and the side wall of the tank. In use the tank may be filled with solution to any level. The cathode is made to oscillate in directions 15, 16 pivoting at 17 in the manner of a pendulum. Movement in the direction 15 causes an increase in solution pressure on that side causing a flow of liquid through gap 7 and formation of a vortex on side 16 with subsequent vigorous agitation of the whole body of solution and most particularly adjacent to the cathode surface. On the return swing the reverse action occurs. The pivot 17 is generally positioned above the solution level and the cathode plate can be detached at this point by releasing wing nut 18. Insulating blocks are fitted at position 19 to prevent any possibility of the anode and cathode touching. Fig. 3 shows a similar tank with two cathode plates. Speeds of oscillation up to 60 per minute have been used. When the plate moves in direction 15 vortices occur in the liquid at 19 and vice versa when moving in the opposite direction. The liquid flow causes the vortices to move towards the centre of the plate. Claims
1. A means of agitating the liquid in a silver recovery system by which the cathode is caused to oscillate about a fixed horizontal axis in the manner of a pendulum, causing the liquid pressure to increase on one side of the plate and to decrease on the opposite side of the plate with subsequent flow of liquid from one side of the plate to the other causing vortices to agitate the cathode surface.
2. A silver recovery agitation system as in Claim 1 with anode and cathode connections reversed.
3. A silver recovery agitation system as in Claim 1 but with two or more oscillating plates.
GB8020182A 1980-06-20 1980-06-20 Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom Withdrawn GB2078782A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB8020182A GB2078782A (en) 1980-06-20 1980-06-20 Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB8020182A GB2078782A (en) 1980-06-20 1980-06-20 Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom

Publications (1)

Publication Number Publication Date
GB2078782A true GB2078782A (en) 1982-01-13

Family

ID=10514191

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8020182A Withdrawn GB2078782A (en) 1980-06-20 1980-06-20 Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom

Country Status (1)

Country Link
GB (1) GB2078782A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0252172A1 (en) * 1986-07-07 1988-01-13 Deutsche Carbone AG Electrolysis process
US5464506A (en) * 1991-09-06 1995-11-07 Eastman Kodak Company Electrolytic device and method having a porous and stirring electrode
DE19543710A1 (en) * 1995-07-25 1997-01-30 Nihon Techno K K Method for treating a fluid by electrolytic oxidation and apparatus for carrying out the method
WO2003054923A2 (en) * 2001-12-20 2003-07-03 Ben-Gurion University Of The Negev A method for packing electrochemically-deposited elements

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0252172A1 (en) * 1986-07-07 1988-01-13 Deutsche Carbone AG Electrolysis process
US5464506A (en) * 1991-09-06 1995-11-07 Eastman Kodak Company Electrolytic device and method having a porous and stirring electrode
DE19543710A1 (en) * 1995-07-25 1997-01-30 Nihon Techno K K Method for treating a fluid by electrolytic oxidation and apparatus for carrying out the method
DE19543710C2 (en) * 1995-07-25 2000-06-15 Nihon Techno K K Apparatus for treating a waste metal liquid containing metal ions and method therefor
WO2003054923A2 (en) * 2001-12-20 2003-07-03 Ben-Gurion University Of The Negev A method for packing electrochemically-deposited elements
WO2003054923A3 (en) * 2001-12-20 2004-03-11 Univ Ben Gurion A method for packing electrochemically-deposited elements

Similar Documents

Publication Publication Date Title
US3964991A (en) Method and apparatus for precipitating colloids from aqueous suspensions
US4790923A (en) Liquid treating electrolytic cell
US4569739A (en) Electrofilter using an improved electrode assembly
US4105534A (en) Apparatus for removing impurities from electrolyte solutions
SE429449B (en) ELECTRIC LIGHT CELL FOR ELECTRIC LIGHT OF THE SEA WATER
US3560366A (en) Ag-o-mat silver recovery unit
GB2078782A (en) Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom
US4075076A (en) Water treatment apparatus
US3278410A (en) Electrolytic anode
US4619747A (en) Electrofilter process using recirculating electrolyte
US4800005A (en) Treatment plant for recovery of metal from hazardous waste
US4022678A (en) Electrolytic cell
US3926768A (en) Silver recovery system
US3436326A (en) Removal of waste solids from aqueous systems
US3356603A (en) Process of treating block liquor with an electrical discharge for the recovery of tall oil
US3464904A (en) Method for treating metallic sulfide compounds
US4417963A (en) Process for removing cyanide ions from solutions
EP0452597A1 (en) Apparatus for electrolytic treatment of liquid media
US3546089A (en) Apparatus for the continuous electrolytic production of chlorine for the sterilization of water
US5017273A (en) Disposable cell for recovering conductive metal and method of using
GB1598306A (en) Electrolytic method and apparatus
US3551317A (en) Electrolytic apparatus for recovering a metal from a solution
JPS62227493A (en) Apparatus for flotation concentration of sludge
GB1437472A (en) Operation of mercury-cathode cells
JPH06510332A (en) Electrolysis device and method with porous stirring electrode

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)