US2073664A - Regeneration of photographic developer solutions - Google Patents
Regeneration of photographic developer solutions Download PDFInfo
- Publication number
- US2073664A US2073664A US688821A US68882133A US2073664A US 2073664 A US2073664 A US 2073664A US 688821 A US688821 A US 688821A US 68882133 A US68882133 A US 68882133A US 2073664 A US2073664 A US 2073664A
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- Prior art keywords
- solution
- developer
- bromide
- development
- photographic
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- Expired - Lifetime
Links
- 230000008929 regeneration Effects 0.000 title description 3
- 238000011069 regeneration method Methods 0.000 title description 3
- 239000000243 solution Substances 0.000 description 71
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 15
- 230000018109 developmental process Effects 0.000 description 13
- 238000000034 method Methods 0.000 description 11
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 230000001172 regenerating effect Effects 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 229910052709 silver Inorganic materials 0.000 description 3
- 239000004332 silver Substances 0.000 description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 229940006460 bromide ion Drugs 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- -1 methyl para aminophenol Chemical compound 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- IOLCXVTUBQKXJR-UHFFFAOYSA-M potassium bromide Chemical compound [K+].[Br-] IOLCXVTUBQKXJR-UHFFFAOYSA-M 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 238000010186 staining Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- PLIKAWJENQZMHA-UHFFFAOYSA-N p-hydroxyphenylamine Natural products NC1=CC=C(O)C=C1 PLIKAWJENQZMHA-UHFFFAOYSA-N 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- ADZWSOLPGZMUMY-UHFFFAOYSA-M silver bromide Chemical compound [Ag]Br ADZWSOLPGZMUMY-UHFFFAOYSA-M 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03C—PHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
- G03C5/00—Photographic processes or agents therefor; Regeneration of such processing agents
- G03C5/26—Processes using silver-salt-containing photosensitive materials or agents therefor
- G03C5/29—Development processes or agents therefor
- G03C5/31—Regeneration; Replenishers
Definitions
- the developer solution consists usually of an organic reducing agent, such as hydroquinone or methyl para aminophenol sulphate, in combination with sodium sulphite, sodium carbonate, and potassium bromide.
- the organic reducing agent is usually referred to as the developer.
- the function of the reducing agent or developer is to convert that part of the silver halide which has been acted on by light to metallic silver.
- the sulphite serves to protect the developer solution from oxidation by the air.
- the carbonate provides the necessary alkalinity.
- the bromide is added as a "restralner, and. its function is to retard the rate of development so as to produce the desired density and contrast.
- One object of this invention is to provide a simple and inexpensive means of regenerating developer solution and reducing the cost oi development.
- Another object of the invention is to provide a method of maintaining substantially uniform developing characteristics in photographic developer solutions.
- Another object of the invention is to provide means of maintaining a substantially uniform temperature in the developing solution regardless of external conditions of temperature.
- Another object of the invention is to provide means of clarifying the developer solution.
- Another object of the invention is to prevent staining which results from the long continued use of developer solutions.
- FIG. 1 illustrates diagrammatically an apparatus which may be used in carrying out the invention
- Fig. 2 is a transverse section through-the electrolytic cell.
- the invention is particularly applicable to large scale industrial operations suchas the development of motion picture film and similar commercial photographic work.
- the developer solution is electrolyzed in a cell, which is divided into two compartments by a suitable diaphragm, the developer solution being in the cathode compartment.
- the anode compartment may contain any suitable electrolyte, such as a solution of sodium hydroxide, sodium carbonate, or sodium sulphate, but we prefer to use a solution which is alkaline.
- a diaphragm we may employ any porous material which prevents mechanical mixing of the solution in the two compartments without preventing the passage of electric current or migration of the bromide ion.
- Suitable diaphragm materials are unglazed porcelain, clay, asbestos, carbon, carborundum, or graphite.
- the cathode is preferably a metal of high hydrogen overvoltage, such as lead or zinc, but other metals, gas carbon or graphite may be employed.
- the anode may be of any metal not attacked by the solution in the anode compartment. In alkaline solution, we prefer to use nickel anodes.
- the electrolytic cell may be made of any suitable material, for example rubber lined steel. Means of agitating the solution during electrolysis are advisable.
- the cathode current density employed varies with the developer used and its concentration, as
- the cathode current density will be regulated so as to give as high current efficiency as possible in reduction of developer.
- the required current density is obtainable with a voltage of approximately 6 to 12 volts.
- the anode current density is not important and may vary within extremely wide limits.
- the temperature at which electrolysis is carried out is subject to wide variation, but preferably the temperature is maintained near the most desirable temperature for development (approximately 60-70 F.).
- the method is utilized most economically in a system involving circulation of the developer solution, it may be applied as a batch operation as well, that is to say, the spent developer solution may be withdrawn and treated in accordance with this invention.
- Such an operation may be used advantageously because treatment in accordance with the invention regenerates the solution and renders it fit for reuse.
- the electrolysis is conducted in a substantially continuous manner, the developer solution being withdrawn continuously from the developer bath or baths, electrolyzed and recirculated so as to maintain the level in the developer bath or baths and likewise to maintain substantially uniform concentrations of developer and bromide in the developer solution.
- the solution is cooled or heated as required to bring it to the right temperature. This facilitates the operation of development and permits obtaining uniformly good results with economy in the use of developer.
- Figure 1 illustrates the layout of the circulation system in which I and 2 indicate tanks through which film is drawn continuously for development.
- the developer solution is fed continuously to the tanks l and 2 from the return pipe 3 and the branch pipes 4 and 5 which are controlled by valves I and I.
- the developer solution is withdrawn continuously through overflow pipes 8 and 8 and delivered through pipe Hi to the cathode compartment of the electrolytic cell II. From the electrolytic cell the solution is withdrawn through an overflow pipe l3 and delivered to the reserve tank ll which is equipped with an agitator l5 and a cooling coil IS. The solution is drawn from the reserve tank through pipe I! by pump l8 and delivered through pipe l9 to filter 20, from which it is returned through pipe 3 for reuse in the developer baths I and Z. A pipe 2
- Additional developer solution to replenish the supply may be maintained in tank 24 and delivered to the reserve tank I 4 through a pipe 25 controlled by a valve 28.
- Additions necessary to maintain the pH of the developer solution may be delivered from tank 21 through pipe 28 controlled by a valve 29 to the reserve tank It.
- the electrolytic cell I2 is equipped with an agitator 30 and a cooling coil 3
- the concentrations of developer and bromide can be maintained so as to give any desired speed of development.
- the current passing through the electrolytic cell shall be regulated so as to take care of fluctuations in the amount of film developed and corresponding changes in the rate at which developer solution is kept flowing through the developer baths.
- the current may be regulated manually, or if preferred, by automatic controlling devices.
- the developer baths can be maintained at the desired temperature, and bromide can be removed continuously and oxidized developer reduced, without impairing or destroying the value of the solution, which is continuously returned for reuse except when the concentration of impurities rises above a predetermined maximum, at which point a portion of the solution can be removed from the system and a suitable supply of replenishing solution can be added.
- the method of regenerating photographic developer solutions which comprises electrolyzing the solution in the cathode compartment of a diaphragm cell and separating bromine in the anode compartment containing an alkaline solution.
- the method of regenerating photographic developer solutions which have become oxidized through use which comprises electrolyzing the oxidized solution in the cathode compartment of a diaphragm electrolytic cell with a potential of from about 6 tov 12 volts.
- the method of regenerating photographic developer solutions which have become oxidized through use which comprises electrolyzing the oxidized solution in the cathode compartment of a diaphragm electrolytic cell with a potential of from about 6 to 12 volts, and while the solution is at a temperature oi about 60 to 70 F.
- the method of regenerating photographic developer solutions which comprises circulating the solution in a cycle including a developing tank, electrolyzing a portion of the solution substantially continuously in the cathode compartment of a diaphragm cell having an alkaline electrolyte in the anode compartment, separating bromine in the anode compartment, and returning the electrolyzed solution to the developing tank.
- the method of maintaining substantially uniform concentrations of developer and bromide in photographic developer solutions which comprises withdrawing a portion of the developer solution from the zone of development, electrolyzing said withdrawn portion of the developer solution in the cathode compartment of a diaphragm electrolytic cell while development is taking place, and at a rate such that reduction of the solution in said cell takes place substantially as fast as the solution is oxidized as the result of the developing operation, and returning LOUIS WEISBERG. WILLARD F. GREENWALD.
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- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Silver Salt Photography Or Processing Solution Therefor (AREA)
- Photographic Processing Devices Using Wet Methods (AREA)
Description
March 16, 1937.
L. WEISBERG ET AL REGENERATION OF PHOTOGRAPHIC DEVELOPER SOLUTIONS Filed Sept. 9, 195:5
REPLENISHING TANK FILTER PUMP DEVELOPING TANK DEVELOPI N6 TANK lo GENERATOR AGITATOR COOLINGTANK g \20 ELEGTROLYT\C CELL INVENTORS ATTORNEYS.
Patented Mar. 16, 1937 UNITED I STATES PATENT OFFICE REGENERATION OF PHOTOGRAPHIG DE- VELOPER SOLUTIONS Louis Weisberg and Willard F. Greenwald, New York, N. Y., assignors, by mesne assignments, to said Willard F. Greenwald Application September 9, 1988, Serial No. 688,821
6 Claims.
I tinuous recirculation.
compensate for these changes. 35.
The methodsemployed in the development of the photographic image are well known. The developer solution consists usually of an organic reducing agent, such as hydroquinone or methyl para aminophenol sulphate, in combination with sodium sulphite, sodium carbonate, and potassium bromide. The organic reducing agent is usually referred to as the developer. The function of the reducing agent or developer is to convert that part of the silver halide which has been acted on by light to metallic silver. The sulphite serves to protect the developer solution from oxidation by the air. The carbonate provides the necessary alkalinity. The bromide is added as a "restralner, and. its function is to retard the rate of development so as to produce the desired density and contrast.
With continued use of the developer solution, the concentration of the developer becomes less on account of the oxidation which takes place. Simultaneously there is an equivalent increase in bromide concentration due to liberation of bromide from. the silver bromide in the emulsion. The decrease in developer concentration and increase in bromide concentration decrease the rate of development. In usual practice, developer is added to the solution at intervals to After the developer solution has been used for some time, it reaches a point where it is no longer economical to continue its use, because increasingly large additions of developer are required to offset the accumulated bromide. By the time this condition is reached, the solution has usually become dark colored and turbid, with a tendency to staining.
One object of this invention is to provide a simple and inexpensive means of regenerating developer solution and reducing the cost oi development.
Another object of the invention is to provide a method of maintaining substantially uniform developing characteristics in photographic developer solutions.
6 Another object of the invention is to provide means of maintaining a substantially uniform temperature in the developing solution regardless of external conditions of temperature.
Another object of the invention is to provide means of clarifying the developer solution.
Another object of the invention is to prevent staining which results from the long continued use of developer solutions.
Other objects and advantages of the-invention will be apparent as it is better understood by reference to the following specification and to the accompanying drawing, in which Fig. 1 illustrates diagrammatically an apparatus which may be used in carrying out the invention; and
Fig. 2 is a transverse section through-the electrolytic cell.
The invention is particularly applicable to large scale industrial operations suchas the development of motion picture film and similar commercial photographic work.
In the practice of the invention, the developer solution is electrolyzed in a cell, which is divided into two compartments by a suitable diaphragm, the developer solution being in the cathode compartment. The anode compartment may contain any suitable electrolyte, such as a solution of sodium hydroxide, sodium carbonate, or sodium sulphate, but we prefer to use a solution which is alkaline. As a diaphragm; we may employ any porous material which prevents mechanical mixing of the solution in the two compartments without preventing the passage of electric current or migration of the bromide ion. Suitable diaphragm materials are unglazed porcelain, clay, asbestos, carbon, carborundum, or graphite. The cathode is preferably a metal of high hydrogen overvoltage, such as lead or zinc, but other metals, gas carbon or graphite may be employed. The anode may be of any metal not attacked by the solution in the anode compartment. In alkaline solution, we prefer to use nickel anodes. The electrolytic cell may be made of any suitable material, for example rubber lined steel. Means of agitating the solution during electrolysis are advisable.
The cathode current density employed varies with the developer used and its concentration, as
well as the concentration of other ingredients in the solution. In practice, the cathode current density will be regulated so as to give as high current efficiency as possible in reduction of developer. The required current density is obtainable with a voltage of approximately 6 to 12 volts. The anode current density is not important and may vary within extremely wide limits. The temperature at which electrolysis is carried out is subject to wide variation, but preferably the temperature is maintained near the most desirable temperature for development (approximately 60-70 F.).
As the electrolysis proceeds the oxidized developer is reduced at the cathode. Bromide, which exists in the solution as bromide ion, travels towards the anode and passes through the diaphragm, out of the developer solution, into the anode compartment. The developer solution becomes lighter in color. Spent developer solution approaches new developer solution in appearance and effectiveness after electrolysis.
While the method is utilized most economically in a system involving circulation of the developer solution, it may be applied as a batch operation as well, that is to say, the spent developer solution may be withdrawn and treated in accordance with this invention. Such an operation may be used advantageously because treatment in accordance with the invention regenerates the solution and renders it fit for reuse.
As an illustration we may describe the result of treating by the present method a batch of developer solution which was almost ready to be thrown away. Before treatment, the developer was very dark and turbid. This turbidity could not be removed by filtration, even with a filter aid. The time required to obtain complete development was three minutes. The solution was electrolyzed at 8 volts for two hours, and then filtered. The filtered solution was about the same color as a new developer solution and perfectly clear. The time required for development with this treated solution was one and onehalf minutes. Film developed for this same time in the untreated solution was considerably underdeveloped.
In the practice of our invention, we prefer to regulate the extent of the electrolysis so as to restore to the developer solution its original developing characteristics. These may be measured by any suitable method, such as the well known H and D curve which shows the relationship between exposure (expressed logarithmically) and the densities produced.
In the preferred and more economical operation of the invention, the electrolysis is conducted in a substantially continuous manner, the developer solution being withdrawn continuously from the developer bath or baths, electrolyzed and recirculated so as to maintain the level in the developer bath or baths and likewise to maintain substantially uniform concentrations of developer and bromide in the developer solution. The solution is cooled or heated as required to bring it to the right temperature. This facilitates the operation of development and permits obtaining uniformly good results with economy in the use of developer.
In carrying out the invention in its preferred form, we may utilize the apparatus illustrated in the accompanying drawing. Figure 1 illustrates the layout of the circulation system in which I and 2 indicate tanks through which film is drawn continuously for development. The developer solution is fed continuously to the tanks l and 2 from the return pipe 3 and the branch pipes 4 and 5 which are controlled by valves I and I.
The developer solution is withdrawn continuously through overflow pipes 8 and 8 and delivered through pipe Hi to the cathode compartment of the electrolytic cell II. From the electrolytic cell the solution is withdrawn through an overflow pipe l3 and delivered to the reserve tank ll which is equipped with an agitator l5 and a cooling coil IS. The solution is drawn from the reserve tank through pipe I! by pump l8 and delivered through pipe l9 to filter 20, from which it is returned through pipe 3 for reuse in the developer baths I and Z. A pipe 2|, connected to the return line, permits the bleeding of any desired portion of the solution in order to avoid excessive accumulation of undesirable impurities. Valves 22 and 23 permit control of the fiow of solution to the bleeder and to the return line.
Additional developer solution to replenish the supply may be maintained in tank 24 and delivered to the reserve tank I 4 through a pipe 25 controlled by a valve 28. Additions necessary to maintain the pH of the developer solution may be delivered from tank 21 through pipe 28 controlled by a valve 29 to the reserve tank It.
The electrolytic cell I2 is equipped with an agitator 30 and a cooling coil 3|, a cathode compartment ll, anode compartment 32, diaphragm 33, cathodes 34 and anodes II.
In the continuous operation of the system as described, the concentrations of developer and bromide can be maintained so as to give any desired speed of development. To maintain a steady, uniform condition it is necessary only that the current passing through the electrolytic cell shall be regulated so as to take care of fluctuations in the amount of film developed and corresponding changes in the rate at which developer solution is kept flowing through the developer baths. The current may be regulated manually, or if preferred, by automatic controlling devices. The developer baths can be maintained at the desired temperature, and bromide can be removed continuously and oxidized developer reduced, without impairing or destroying the value of the solution, which is continuously returned for reuse except when the concentration of impurities rises above a predetermined maximum, at which point a portion of the solution can be removed from the system and a suitable supply of replenishing solution can be added.
It is evident that the invention is applicable to other salts of silver which may be used in photographic emulsions, and the term bromide as employed in the claims is intended to cover any ion which is equivalent to or used in place of bromide.
Various changes may be made in the details of construction and arrangement of the apparatus and the procedure without departing from the invention or sacrificing any of its advantages.
We claim:
1. The method of regenerating photographic developer solutions which comprises electrolyzing the solution in the cathode compartment of a diaphragm cell and separating bromine in the anode compartment containing an alkaline solution.
2. The method of regenerating photographic developer solutions which have become oxidized through use which comprises electrolyzing the oxidized solution in the cathode compartment of a diaphragm electrolytic cell with a potential of from about 6 tov 12 volts.
3. The method of regenerating photographic developer solutions which have become oxidized through use which comprises electrolyzing the oxidized solution in the cathode compartment of a diaphragm electrolytic cell with a potential of from about 6 to 12 volts, and while the solution is at a temperature oi about 60 to 70 F.
4. The method of regenerating photographic developer solutions which comprises circulating the solution in a cycle including a developing tank, electrolyzing a portion of the solution substantially continuously in the cathode compartment of a diaphragm cell having an alkaline electrolyte in the anode compartment, separating bromine in the anode compartment, and returning the electrolyzed solution to the developing tank.
5. The method of maintaining substantially uniform concentrations of developer and bromide in photographic developer solutions which ing at least a portion of the developer solution in the cathode compartment of a diaphragm electrolytic cell at a rate such that reduction of the solution in said cell takes place substantially as fast as the solution is oxidized as the result of the developing operation.
'6. The method of maintaining substantially uniform concentrations of developer and bromide in photographic developer solutions which comprises withdrawing a portion of the developer solution from the zone of development, electrolyzing said withdrawn portion of the developer solution in the cathode compartment of a diaphragm electrolytic cell while development is taking place, and at a rate such that reduction of the solution in said cell takes place substantially as fast as the solution is oxidized as the result of the developing operation, and returning LOUIS WEISBERG. WILLARD F. GREENWALD.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US688821A US2073664A (en) | 1933-09-09 | 1933-09-09 | Regeneration of photographic developer solutions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US688821A US2073664A (en) | 1933-09-09 | 1933-09-09 | Regeneration of photographic developer solutions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2073664A true US2073664A (en) | 1937-03-16 |
Family
ID=24765925
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US688821A Expired - Lifetime US2073664A (en) | 1933-09-09 | 1933-09-09 | Regeneration of photographic developer solutions |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2073664A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2549099A (en) * | 1947-07-14 | 1951-04-17 | Fabric Res Lab Inc | Process for stripping color from dyed wool |
| US3978506A (en) * | 1973-12-07 | 1976-08-31 | Agfa-Gevaert, A.G. | Apparatus and method for neutralizing waste photographic fluids |
| US3998710A (en) * | 1975-03-11 | 1976-12-21 | The Japan Carlit Co., Ltd. | Process for electrolytically purifying a photographic waste solution |
| US4025344A (en) * | 1972-08-31 | 1977-05-24 | E. I. Du Pont De Nemours And Company | Lithographic developer replenishment process |
| US4081816A (en) * | 1973-12-07 | 1978-03-28 | Agfa-Gevaert, A.G. | Apparatus for processing photographic film and treating contaminated processing liquids |
| US4128424A (en) * | 1973-12-07 | 1978-12-05 | Agfa-Gevaert Ag | Method for treating photographic processing fluids prior to sewering thereof |
| US4147601A (en) * | 1977-07-28 | 1979-04-03 | Ppg Industries, Inc. | Electrolytic production of hydrobromic acid |
| US4151062A (en) * | 1978-01-04 | 1979-04-24 | Norris Richard J | Metals recovery apparatus |
| US4278515A (en) * | 1979-10-15 | 1981-07-14 | The United States Of America As Represented By The Secretary Of The Army | Method for removal of sodium carbonate from cyanide plating baths |
| US4365481A (en) * | 1979-10-15 | 1982-12-28 | The United States Of America As Represented By The Secretary Of The Army | Method and apparatus for removal of sodium carbonate from cyanide plating baths |
-
1933
- 1933-09-09 US US688821A patent/US2073664A/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2549099A (en) * | 1947-07-14 | 1951-04-17 | Fabric Res Lab Inc | Process for stripping color from dyed wool |
| US4025344A (en) * | 1972-08-31 | 1977-05-24 | E. I. Du Pont De Nemours And Company | Lithographic developer replenishment process |
| US3978506A (en) * | 1973-12-07 | 1976-08-31 | Agfa-Gevaert, A.G. | Apparatus and method for neutralizing waste photographic fluids |
| US4081816A (en) * | 1973-12-07 | 1978-03-28 | Agfa-Gevaert, A.G. | Apparatus for processing photographic film and treating contaminated processing liquids |
| US4128424A (en) * | 1973-12-07 | 1978-12-05 | Agfa-Gevaert Ag | Method for treating photographic processing fluids prior to sewering thereof |
| US4160594A (en) * | 1973-12-07 | 1979-07-10 | Agfa-Gevaert, A.G. | Method and arrangement for the development of latent images particularly latent photographic images |
| US3998710A (en) * | 1975-03-11 | 1976-12-21 | The Japan Carlit Co., Ltd. | Process for electrolytically purifying a photographic waste solution |
| US4147601A (en) * | 1977-07-28 | 1979-04-03 | Ppg Industries, Inc. | Electrolytic production of hydrobromic acid |
| US4151062A (en) * | 1978-01-04 | 1979-04-24 | Norris Richard J | Metals recovery apparatus |
| US4278515A (en) * | 1979-10-15 | 1981-07-14 | The United States Of America As Represented By The Secretary Of The Army | Method for removal of sodium carbonate from cyanide plating baths |
| US4365481A (en) * | 1979-10-15 | 1982-12-28 | The United States Of America As Represented By The Secretary Of The Army | Method and apparatus for removal of sodium carbonate from cyanide plating baths |
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