EP0965883A1 - Ecological cleaning liquid for photographic processor - Google Patents

Ecological cleaning liquid for photographic processor Download PDF

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Publication number
EP0965883A1
EP0965883A1 EP98202038A EP98202038A EP0965883A1 EP 0965883 A1 EP0965883 A1 EP 0965883A1 EP 98202038 A EP98202038 A EP 98202038A EP 98202038 A EP98202038 A EP 98202038A EP 0965883 A1 EP0965883 A1 EP 0965883A1
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EP
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Prior art keywords
silver
cleaning
iii
salt
mole
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German (de)
French (fr)
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Agfa Gevaert NV
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Agfa Gevaert NV
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Priority to EP98202038A priority Critical patent/EP0965883A1/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/34Organic compounds containing sulfur
    • C11D3/349Organic compounds containing sulfur additionally containing nitrogen atoms, e.g. nitro, nitroso, amino, imino, nitrilo, nitrile groups containing compounds or their derivatives or thio urea
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/26Organic compounds containing nitrogen
    • C11D3/33Amino carboxylic acids
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C11/00Auxiliary processes in photography
    • G03C11/005Cleaning photographic processing and manufacturing apparatus
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D2111/00Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
    • C11D2111/10Objects to be cleaned
    • C11D2111/14Hard surfaces
    • C11D2111/20Industrial or commercial equipment, e.g. reactors, tubes or engines
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/34Organic compounds containing sulfur
    • C11D3/3427Organic compounds containing sulfur containing thiol, mercapto or sulfide groups, e.g. thioethers or mercaptales

Definitions

  • the present invention deals with an improved ecological one-step cleaning liquid for photographic processing equipment.
  • deposits can form on the walls of the various processor tanks and on the mechanical roller/belt system used to transport the photographic silver halide material through the processor. These deposits are likely to soil the next sheets or stripes of processed film or paper.
  • the deposits can be metallic silver, commonly referred to as “silver sludge", insoluble silver salts and alkali metal salts.
  • the deposits in the fixer tank can be silver salts, alkali metal salts, aluminum oxides and elemental sulphur.
  • the deposits in the wash tanks can be alkali metal salts, gelatin and gelatin by-products which induce the growth of fungi and algae.
  • the prior art utilizes different cleaning compositions for the various tanks.
  • the developer tank requires a combination of a strong oxidizing agent and a silver solvent system.
  • Commonly used prior art cleaning solutions contained chromate salts such as dichromate combined with sulphuric or sulphamic acid (see e.g. DE 1068840). Consecutively a neutralizer such as an alkali bisulfite solution was used to remove residual chromate salts.
  • a strong caustic solution is used to dissolve the salts and silver complexes.
  • the algae and fungi slime in the wash tanks can be cleaned by a chlorine bleach such as a hypochlorite solution. From a modern ecological point of view all the chemicals cited above are agressive and hazardous to the environment.
  • Chromium is recognized as a pollutant and a potential carcinogen.
  • Caustic solutions are very injurious to the eyes and skin.
  • the hypochlorite solution for cleaning the wash tank can react with residual caustic solution, used for the fixer, giving rise to the formation of toxic gaseous chlorine.
  • the cleaning composition contains hydrogen ions, ammonium ions and sulphate ions.
  • it is composed of sulphuric acid, ferric ammonium sulphate and water.
  • CA 734388 a five-steps process is disclosed for cleaning successively all sections of an automatic processor.
  • an aqueous solution with a pH of at most 1.0 and containing cerium(IV) ions is used, which however is corrosive.
  • US 4,021,264 silver deposits are removed with an aqueous solution containing an alkali mono- or di-peroxysulphate, an alkali bisulphate and thiourea.
  • the latter substance can cause photographic fog.
  • a cleaning liquid containing a peroxydisulphate compound, an iron(III) salt and optionally an activator.
  • JP-A 58-048052 describes an acidic cleaning solutiuon containing iodide or bromide ions.
  • the cleaning composition comprises water, a hydroxycarboxylic acid such as citric acid or tartaric acid, and a peroxymonosulphate compound.
  • a method for cleaning photographic treating equipment with a solution containing an aminopolycarboxylic acid ferric chelate and a silver complexing agent is disclosed in JP-A 2-311845.
  • a two-steps cleaning metod is described using a first composition containing a chelate of an iron(III) salt plus a complexing agent, and a second composition which comprises water, an acid or acid anhydride, a surfactant and a water soluble solvent.
  • the aqueous cleaning composition contains a peroxocompound, preferably sodium persulphate; in most examples sulfamic acid is also present.
  • the present invention extends the teachings on cleaning liquids for photographic processors. It is an object of the present invention to provide an
  • an aqueous cleaning composition for a photographic processor comprising,
  • a monophosphate salt e.g. an alkali monophosphate salt, is also present in the cleaning composition.
  • a principal ingredient of the cleaning composition according to the present invention is an aminopolycarboxylic acid chelate of an iron(III) salt.
  • This compound will take care of the oxidation of the metallic silver sludge to silver ions.
  • Suitable chelating agents for iron(III) ions are EDTA, DTPA, hydroxy(EDTA), PDTA, MIDA, ADA and NTA.
  • the four latter compounds show the advantage of being biodegradable.
  • Preferred compounds are sodium iron(III) EDTA, and ammonium iron(III) EDTA.
  • the most preferred compound is ammonium iron(III) EDTA.
  • the concentration of the iron complex salt must be at least 0.01 mole/l in order to be effective, and is preferably comprised between 0.025 and 0.2 mole/l.
  • Suitable silver complexing agents include sodium-, potassium-, and ammonium thiosulphate; sodium-, potassium- or ammonium thiocyanate; sodium dithionate; alkyl alkanolamines; alkyl amines; thiourea; alkyl thiourea; cysteine HCl; ammonium dithiocarbamate.
  • the most preferred silver complexing agent is ammonium thiosulphate.
  • Another preferred silver complexing agent is dithiaoctanediol.
  • the concentration of the silver complexing agent must be at least 0.05 mole/l.
  • An essential ingredient of the cleaning composition according to the present invention is a silver oxidizing accelerator belonging to a specific chemical class.
  • This compound is an organic heterocyclic compound having at least two nitrogen atoms in the heterocyclic nucleus and carrying a mercapto group.
  • Highly preferred silver oxidation accelerators according to the defined class include the compounds of following table 1 :
  • the most preferred silver oxidation accelerator is 3-mercapto-1,2,4-triazole (compound 3).
  • the concentration of the silver oxidation accelerator in the cleaning solution must be at least 0.001 mole/l, and is preferably comprised between 0.005 and 0.05 mole/l.
  • a silver oxidation accelerator as defined above it was necessary to use high concentrations of the chelated iron(III) salt, and the presence of a monophosphate salt was indispensable. Thanks to the presence of the silver oxidation accelerator moderate concentrations of the chelated iron(III) salt can be used and the presence of a monophosphate salt becomes optional.
  • a monophosphate salt is present preferably in a concentration between 0.02 and 0.15 mole/l.
  • the monophosphate ion functions as a supplementary oxidation accelerator and at the same time as a buffer substance.
  • the monophosphate salt is an alkali salt, e.g. potassium monophosphate or sodium monophosphate.
  • the cleaning solution can further optionally contain several other kinds of ingredients.
  • the composition can contain minor amounts of inorganic or organic acids, such as acetic acid and/or citric acid, in order to adjust the pH of the cleaning solution and strenghten the buffer capacity.
  • the pH of the cleaning composition is preferably comprised between 4 and 7.
  • the solution can further contain a sequestering agent for complexing calcium and magnesium ions originating from hard water.
  • the solution can further contain sulphite ions, preferably potassium sulphite. It assures the stabilisation of the thiosulphate.
  • the solution can further contain one or more surfactants in order to assure good spreading activity on processor surfaces and good dispersion of silver deposits.
  • a practical cleaning test is performed as follows.
  • An automatic Rapiline 66 processor (registered trademark of Agfa-Gevaert N.V.) was filled with a conventional hydroquinone/Phenidone developer and a conventional fixer.
  • About 80 m 2 of negative working red sensitive imagesetting film was processed with 50 ml/m 2 replenishment in dark light conditions to obtain clear film and to contaminate as much as possible the developer with dissolved silver halide.
  • the cleaning solution was put in (ready-for-use, as concentrate, or as powder) and the processor ran for 15 minutes with the cleaning solution at 23°C. Thereafter the cleaning solution was drained and the developing tank was rinsed twice with tap water at room temperature. There is no second cleaning phase necessary. The tank was drained and the rollers, guiding plates and walls where controlled on remaining black silver deposit. The results where quoted from 0 to 5 according to an arbitrary scale. Zero means that no remaining silver deposit was found. Five means no reduction in silver deposit with regard to the start of the cleaning.
  • a typical developer tank consists of the tank and the developer rack.
  • the developer rack has the transport function for the immersed photographic material. This means that the possible appearance of scratches, guiding plate marks and roller marks is dependent on the quality of the rack.
  • the entrance and the exit roller pair are the places where silver sludge contamination is most apparent, but the bottom guiding plate and rollers are the most contaminated ones.
  • the most common places where silver sludge is transferred on the photographic material are the rollers (cause pressure and slip) and the guiding plates (cause abration due to direct contact). To prevent this heavily disturbing problem chemical cleaning of the developer is necessary as decribed here.
  • Racks are to complex to clean mechanically. Also in closed tank and small guiding sleeves systems chemical cleaning at the spot is the only solution.
  • This example illustrates the efficiency of the presence of several different silver oxidation accelerators and compares there activity by means of a bleach-fix test.
  • This test is performed as follows. After 25 s of immersion in bright light in a conventional developer, and immersion in a fixer in an automatic Rapiline 66 processor of the photographic red sensitive, negative working recording paper Alliance HNp, having a silver coverage of 2.2 g/m 2 , a maximum density of above 2.00 is reached. The roll material was cut in small strips of about 3x10cm. The strips where partially immersed in 250ml of different stirred cleaning solutions at room temperature. The time of immersion was 60, 50, 40, 30, 20, 10 and 0 seconds respectively.
  • the strips where rinsed in tap water (stop function) and consequetively rinsed in fixer and tap water, and dried.
  • the reflection density was measured with a MacBeth RD918 densitometer to follow the bleach-fixing activity and the results where put in a graph.
  • the (interpolated) time to reach a density of 0.5 was taken as representative. A time shorter than 40 seconds is considered as good.
  • the actual cleaning compositions contained 0.194 mole/l ammonium Fe(III)EDTA, 0.336 mole/l ammonium thiosulphate, 0.083 mole/l potassium sulphite, 0.022 mole/l of Na-sequestrene, and 0.01 mol/l of the different silver oxidation accelerators.
  • the pH was adjusted to 5.5 with acetic acid.
  • the interpolated times to reach a reflection density of 0.5 are illustrated in following table 2a.
  • compound No. time (s) D 0.5 cmpd 1 38 cmpd 2 29 cmpd 3 33 cmpd 4 36 cmpd 5 36 cmpd 6 38 cmpd 7 36 cmpd 8 28 cmpd 9 29 - (blank) 47
  • Table 2b shows the bleach-fix speed of a liquid containing compound 3 compared to a blank containing no oxidation accelerator.
  • time s
  • Density blade
  • Density cmpd 3

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Abstract

An improved ecological one-step cleaning liquid for photographic processing equipment is disclosed. The aqueous solution comprises (1) an aminopolycarboxylic acid chelate of an iron(III) salt, (2) a silver complexing agent, and (3) a silver oxidation accelerator of a particular type. Preferably, also a monophosphate salt is present.

Description

FIELD OF THE INVENTION
The present invention deals with an improved ecological one-step cleaning liquid for photographic processing equipment.
BACKGROUND OF THE INVENTION
As it is well known conventional black-and-white photographic processing involves the consecutive use of at least three solutions being a developer which reduces the silver halide grains carrying a latent image to metallic silver, a fixing solution to remove undeveloped silver halide, and finally a wash tank to remove residual fixer. In manual tray processing a stop bath can be inserted between developer and fixer to arrest the developer, but this is usually omitted in an automatic mechanical processor by providing the fixer with a high buffering capacity.
After prolonged continuous processing unwanted deposits can form on the walls of the various processor tanks and on the mechanical roller/belt system used to transport the photographic silver halide material through the processor. These deposits are likely to soil the next sheets or stripes of processed film or paper. In the developer tank the deposits can be metallic silver, commonly referred to as "silver sludge", insoluble silver salts and alkali metal salts. In the fixer tank the deposits can be silver salts, alkali metal salts, aluminum oxides and elemental sulphur. Finally, the deposits in the wash tanks can be alkali metal salts, gelatin and gelatin by-products which induce the growth of fungi and algae.
The prior art utilizes different cleaning compositions for the various tanks. The developer tank requires a combination of a strong oxidizing agent and a silver solvent system. Commonly used prior art cleaning solutions contained chromate salts such as dichromate combined with sulphuric or sulphamic acid (see e.g. DE 1068840). Consecutively a neutralizer such as an alkali bisulfite solution was used to remove residual chromate salts. In cleaning the fixer tank a strong caustic solution is used to dissolve the salts and silver complexes. The algae and fungi slime in the wash tanks can be cleaned by a chlorine bleach such as a hypochlorite solution. From a modern ecological point of view all the chemicals cited above are agressive and hazardous to the environment. Chromium is recognized as a pollutant and a potential carcinogen. Caustic solutions are very injurious to the eyes and skin. The hypochlorite solution for cleaning the wash tank can react with residual caustic solution, used for the fixer, giving rise to the formation of toxic gaseous chlorine.
Various alternatives have been formulated in the prior art to substitute the cleaning chemicals described above.
According to US 3,625,908 the cleaning composition contains hydrogen ions, ammonium ions and sulphate ions. In the preferred embodiment it is composed of sulphuric acid, ferric ammonium sulphate and water. In CA 734388 a five-steps process is disclosed for cleaning successively all sections of an automatic processor. According to DE 2429833 an aqueous solution with a pH of at most 1.0 and containing cerium(IV) ions is used, which however is corrosive. In US 4,021,264 silver deposits are removed with an aqueous solution containing an alkali mono- or di-peroxysulphate, an alkali bisulphate and thiourea. However, the latter substance can cause photographic fog. In DE 2756010 a cleaning liquid is disclosed containing a peroxydisulphate compound, an iron(III) salt and optionally an activator. JP-A 58-048052 describes an acidic cleaning solutiuon containing iodide or bromide ions. According to US 4,678,597 the cleaning composition comprises water, a hydroxycarboxylic acid such as citric acid or tartaric acid, and a peroxymonosulphate compound. A method for cleaning photographic treating equipment with a solution containing an aminopolycarboxylic acid ferric chelate and a silver complexing agent is disclosed in JP-A 2-311845. In US 5,266,121 a two-steps cleaning metod is described using a first composition containing a chelate of an iron(III) salt plus a complexing agent, and a second composition which comprises water, an acid or acid anhydride, a surfactant and a water soluble solvent. In US 5,441,665 the aqueous cleaning composition contains a peroxocompound, preferably sodium persulphate; in most examples sulfamic acid is also present.
OBJECTS OF THE INVENTION
The present invention extends the teachings on cleaning liquids for photographic processors. It is an object of the present invention to provide an
ecologically acceptable cleaning composition for a photographic processor.
It is a further object of the present invention to provide a cleaning composition for a photographic processor with reduced cleaning time.
It is still a further object of the present invention to provide a cleaning composition which is suitable for cleaning the developer tank in just one step.
SUMMARY OF THE INVENTION
The above mentioned objects are realised by providing an aqueous cleaning composition for a photographic processor comprising,
  • (1) an aminopolycarboxylic acid chelate of an iron(III) salt in a concentration of at least 0.01 mole/l,
  • (2) a silver complexing agent in a concentration of at least 0.05 mole/l,
  • (3) a heterocyclic silver oxidation accelerating compound having at least two nitrogen atoms in the heterocyclic nucleus and carrying a mercapto group and not carrying a hydrophilic substituent besides said mercapto group, in a concentration of at least 0.001 mole/l.
  • In a preferred embodiment also a monophosphate salt, e.g. an alkali monophosphate salt, is also present in the cleaning composition.
    DETAILED DESCRIPTION OF THE INVENTION
    A principal ingredient of the cleaning composition according to the present invention is an aminopolycarboxylic acid chelate of an iron(III) salt. This compound will take care of the oxidation of the metallic silver sludge to silver ions. Suitable chelating agents for iron(III) ions are EDTA, DTPA, hydroxy(EDTA), PDTA, MIDA, ADA and NTA. The four latter compounds show the advantage of being biodegradable. Preferred compounds are sodium iron(III) EDTA, and ammonium iron(III) EDTA. The most preferred compound is ammonium iron(III) EDTA. The concentration of the iron complex salt must be at least 0.01 mole/l in order to be effective, and is preferably comprised between 0.025 and 0.2 mole/l.
    Suitable silver complexing agents include sodium-, potassium-, and ammonium thiosulphate; sodium-, potassium- or ammonium thiocyanate; sodium dithionate; alkyl alkanolamines; alkyl amines; thiourea; alkyl thiourea; cysteine HCl; ammonium dithiocarbamate. The most preferred silver complexing agent is ammonium thiosulphate. Another preferred silver complexing agent is dithiaoctanediol. The concentration of the silver complexing agent must be at least 0.05 mole/l.
    An essential ingredient of the cleaning composition according to the present invention is a silver oxidizing accelerator belonging to a specific chemical class. This compound is an organic heterocyclic compound having at least two nitrogen atoms in the heterocyclic nucleus and carrying a mercapto group. Highly preferred silver oxidation accelerators according to the defined class include the compounds of following table 1 :
    Figure 00040001
    Figure 00050001
    The most preferred silver oxidation accelerator is 3-mercapto-1,2,4-triazole (compound 3).
    The concentration of the silver oxidation accelerator in the cleaning solution must be at least 0.001 mole/l, and is preferably comprised between 0.005 and 0.05 mole/l.
    It was found experimentally that when a silver oxidation accelerator as defined above was omitted it was necessary to use high concentrations of the chelated iron(III) salt, and the presence of a monophosphate salt was indispensable. Thanks to the presence of the silver oxidation accelerator moderate concentrations of the chelated iron(III) salt can be used and the presence of a monophosphate salt becomes optional. However, in a preferred embodiment of the present invention a monophosphate salt is present preferably in a concentration between 0.02 and 0.15 mole/l. The monophosphate ion functions as a supplementary oxidation accelerator and at the same time as a buffer substance. Preferably the monophosphate salt is an alkali salt, e.g. potassium monophosphate or sodium monophosphate.
    The cleaning solution can further optionally contain several other kinds of ingredients.
    The composition can contain minor amounts of inorganic or organic acids, such as acetic acid and/or citric acid, in order to adjust the pH of the cleaning solution and strenghten the buffer capacity. The pH of the cleaning composition is preferably comprised between 4 and 7.
    The solution can further contain a sequestering agent for complexing calcium and magnesium ions originating from hard water.
    The solution can further contain sulphite ions, preferably potassium sulphite. It assures the stabilisation of the thiosulphate.
    The solution can further contain one or more surfactants in order to assure good spreading activity on processor surfaces and good dispersion of silver deposits.
    A practical cleaning test is performed as follows. An automatic Rapiline 66 processor (registered trademark of Agfa-Gevaert N.V.) was filled with a conventional hydroquinone/Phenidone developer and a conventional fixer. About 80 m2 of negative working red sensitive imagesetting film was processed with 50 ml/m2 replenishment in dark light conditions to obtain clear film and to contaminate as much as possible the developer with dissolved silver halide. After a period of sedimentation (1-3 days) the developing tank, rollers, guiding plates and walls were completely turned black and gray ("silver mirror" effect). Than the developer tank was drained. The cleaning solution was put in (ready-for-use, as concentrate, or as powder) and the processor ran for 15 minutes with the cleaning solution at 23°C. Thereafter the cleaning solution was drained and the developing tank was rinsed twice with tap water at room temperature. There is no second cleaning phase necessary. The tank was drained and the rollers, guiding plates and walls where controlled on remaining black silver deposit. The results where quoted from 0 to 5 according to an arbitrary scale. Zero means that no remaining silver deposit was found. Five means no reduction in silver deposit with regard to the start of the cleaning.
    The cleaning system described is suitable for all types of photographic processors. A typical developer tank consists of the tank and the developer rack. In the tank there are sensors, heating elements, drain and replenishing pipes and circulation holes. The corners and surface around these elements are very hard to clean mechanically; only chemical cleaning is effective. The developer rack has the transport function for the immersed photographic material. This means that the possible appearance of scratches, guiding plate marks and roller marks is dependent on the quality of the rack. The entrance and the exit roller pair are the places where silver sludge contamination is most apparent, but the bottom guiding plate and rollers are the most contaminated ones. The most common places where silver sludge is transferred on the photographic material are the rollers (cause pressure and slip) and the guiding plates (cause abration due to direct contact). To prevent this heavily disturbing problem chemical cleaning of the developer is necessary as decribed here. Racks are to complex to clean mechanically. Also in closed tank and small guiding sleeves systems chemical cleaning at the spot is the only solution.
    The present invention will now be illustrated by the following examples without however being limited thereto.
    EXAMPLES Example 1
    This example illustrates the efficiency of the presence of several different silver oxidation accelerators and compares there activity by means of a bleach-fix test. This test is performed as follows. After 25 s of immersion in bright light in a conventional developer, and immersion in a fixer in an automatic Rapiline 66 processor of the photographic red sensitive, negative working recording paper Alliance HNp, having a silver coverage of 2.2 g/m2, a maximum density of above 2.00 is reached. The roll material was cut in small strips of about 3x10cm. The strips where partially immersed in 250ml of different stirred cleaning solutions at room temperature. The time of immersion was 60, 50, 40, 30, 20, 10 and 0 seconds respectively. The strips where rinsed in tap water (stop function) and consequetively rinsed in fixer and tap water, and dried. The reflection density was measured with a MacBeth RD918 densitometer to follow the bleach-fixing activity and the results where put in a graph. The (interpolated) time to reach a density of 0.5 was taken as representative. A time shorter than 40 seconds is considered as good.
    The actual cleaning compositions contained 0.194 mole/l ammonium Fe(III)EDTA, 0.336 mole/l ammonium thiosulphate, 0.083 mole/l potassium sulphite, 0.022 mole/l of Na-sequestrene, and 0.01 mol/l of the different silver oxidation accelerators. The pH was adjusted to 5.5 with acetic acid. The interpolated times to reach a reflection density of 0.5 are illustrated in following table 2a.
    compound No. time (s) D=0.5
    cmpd 1 38
    cmpd 2 29
    cmpd 3 33
    cmpd 4 36
    cmpd 5 36
    cmpd 6 38
    cmpd 7 36
    cmpd 8 28
    cmpd 9 29
    - (blank) 47
    The table shows that all the tested compound are effective (time to reach D=0.5 smaller than 40 s).
    Table 2b shows the bleach-fix speed of a liquid containing compound 3 compared to a blank containing no oxidation accelerator.
    time (s) Density (blank) Density (cmpd 3)
    0 2.04 2.02
    10 1.89 1.71
    20 1.34 1.17
    30 1.05 0.55
    40 0.66 0.38
    50 0.43 0.39
    It is clear from table 2b that the bleach-fixing is performed faster with a liquid containing compound 3.
    As comparison we give hereinafter the results of the bleach-fix test (densities) performed with two prior art cleaning liquids the oxidation step of which was based on bichromate (cleaning liquid A) and on persulphate (cleaning liquid B) respectively. In both cases a second step being a complexing step was necessary.
    bleachfix time cl. liq. A cl. liq. B
    10.s 0.35 1.99
    20.s 0.35 2.01
    30 s 0.35 1.97
    40 s 0.37 1.94
    60.s 0.34 1.85
    t(D=0.5)= <10 s >60 s
    Tank cleaning: 0 (15'/23°C) 5 (arbitrary scale)
    The molar compositions of cleaning liquid A and cleaning liquid B were as follows :
    PHASE 1: oxidation/bleaching
    compound conc mole/l conc mole/l
    H2SO4 0.108 0
    sulfaminic acid 0.268 0
    K2Cr2O7 0.041 0
    NaOH 0 0.100
    CH3COOH 0 0.347
    Hydroquinone 0 0.036
    KBr 0 0.084
    ammoniumpersulphate 0 0.132
    PHASE 2: Complexing phase
    compound conc mole/l conc mole/l
    (NH4)2S2O3 0.925 0.701
    Na2SO3 0.086 0
    H3BO3 0.081 0
    CH3COONa 0.103 0
    CH3COOH 0.138 0
    One sees that the bleach-fixing speed is all right for the cleaning liquid based on bichromate, which however is unecologig, but much too slow for the liquid based on persulphate. However, both comparative systems show the disadvantage of requiring a second step being a complexing phase.
    Example 2
    In example 2 the cleaning efficiency of cleaning solutions having different compositions are compared. The results are summarized in tables 3a and 3b.
    ingredient molar concentrations
    C1 C2 I1 I2 I3 I4 I5 I6
    Na-sequestrene 0.022 = = = = = = =
    K2SO3 0.083 = = = = = = =
    cpd 3 - - 0.050 0.050 0.030 0.010 0.005 0.010
    HAc 0.606 0.606 0.628 0.491 0.471 0.471 0.626 0.583
    (NH4)2S2O3 0.336 0.637 0.336 = = = = =
    NaH2PO4.2aq 0.096 = = = = = = 0
    NH4Fe(III)EDTA 0.388 = = = = = = =
    pH 5.11 5.11 5.11 5.50 5.50 5.50 5.11 5.50
    cleaning quality 3 5 0 0 0 0 0 0.5
    As already explained above the quality of the cleaning is qualitatively rated by an arbitrary scale ranging from 0 (very good) to 5 (very bad). It is clear from the table that the comparison examples (C1 and C2) containing no silver oxidation accelerator show a worse cleaning result than the invention examples (I1-I6). The example containing no sodium monophosphate gives a slightly worse result than the corresponding probe containing monophosphate.
    ingredients molar concentration
    I6 I7 I8 I9 I10 C3
    Na-sequestrene 0.022 = = = = =
    K2SO3 0.083 = = = = =
    cmpd 3 0.010 0.005 0.010 = = =
    HAc 0.538 0.223 0.208 0.163 0.147 0.270
    (NH4)2S2O3 0.336 = = = = =
    NaH2PO4.2aq 0 0.032 0.096 = = =
    NH4Fe(III)EDTA 0.388 0.194 0.097 0.048 0.024 0.006
    pH 5.50 4.45 5.50 = = =
    cleaning quality 0.5 0.5 0 0 0 3
    It is clear from table 3b that the presence and the concentration of the iron(III) complex salt is of crucial importance for the quality of the cleaning. A concentration as low as 0.006 is ineffective (comparison example C3). The examples without or with a low concentration on sodium monophosphate show again a slightly worse behaviour even at relative high concentrations of NH4Fe(III)EDTA.

    Claims (6)

    1. An aqueous cleaning composition for a photographic processor comprising,
      (1) an aminopolycarboxylic acid chelate of an iron(III) salt in a concentration of at least 0.01 mole/l,
      (2) a silver complexing agent in a concentration of at least 0.05 mole/l,
      (3) a heterocyclic silver oxidation accelerating compound having at least two nitrogen atoms in the heterocyclic nucleus and carrying a mercapto group, in a concentration of at least 0.001 mole/l.
    2. An aqueous cleaning composition according to claim 1 wherein said aminopolycarboxylic acid chelate of an iron(III) salt is an EDTA chelate.
    3. An aqueous cleaning composition according to claim 2 wherein said EDTA chelate is chosen from ammonium iron(III) EDTA and sodium iron(III) EDTA.
    4. An aqueous cleaning composition according to any of claims 1 to 3 wherein said silver compexing agent is a thiosulphate.
    5. An aqueous cleaning composition according to any of claims 1 to 4 wherein said silver oxidation accelerating compound is 3-mercapto-1,2,4-triazole.
    6. An aqueous cleaning composition according to any of claims 1 to 5 wherein said composition further contains a monophosphate salt.
    EP98202038A 1998-06-18 1998-06-18 Ecological cleaning liquid for photographic processor Withdrawn EP0965883A1 (en)

    Priority Applications (1)

    Application Number Priority Date Filing Date Title
    EP98202038A EP0965883A1 (en) 1998-06-18 1998-06-18 Ecological cleaning liquid for photographic processor

    Applications Claiming Priority (1)

    Application Number Priority Date Filing Date Title
    EP98202038A EP0965883A1 (en) 1998-06-18 1998-06-18 Ecological cleaning liquid for photographic processor

    Publications (1)

    Publication Number Publication Date
    EP0965883A1 true EP0965883A1 (en) 1999-12-22

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    EP (1) EP0965883A1 (en)

    Cited By (1)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    CN113900349A (en) * 2021-10-25 2022-01-07 陕西师范大学 Method for removing silver mirror on surface layer of black and white negative film

    Citations (8)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    CH490696A (en) * 1965-06-11 1970-05-15 Agfa Gevaert Ag Process for producing color photographic images
    DE2102713A1 (en) * 1971-01-21 1972-08-10 Agfa-Gevaert Ag, 5090 Leverkusen Hardening bleach-fix baths
    FR2241095A1 (en) * 1973-08-16 1975-03-14 Eastman Kodak Co
    US4914009A (en) * 1986-06-30 1990-04-03 Fuji Photo Film Co., Ltd. Process for forming direct positive color image comprising the use of bleach accelerators
    DE4034873A1 (en) * 1990-11-02 1992-05-07 Wolfen Filmfab Ag Photographic colour bleaching bath prodn. - by adding accelerator of 3-mercapto-s-triazole to conc soln., for silver halide gelatin emulsion
    US5266121A (en) * 1992-08-12 1993-11-30 Helion Industries, Inc. Method of cleaning photographic processing equipment
    US5464727A (en) * 1995-02-08 1995-11-07 Eastman Kodak Company Cleaning of emulsion manufacturing apparatus
    US5476593A (en) * 1994-12-08 1995-12-19 Eastman Kodak Company Method for flushing an undesired precipitate from apparatus surfaces

    Patent Citations (8)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    CH490696A (en) * 1965-06-11 1970-05-15 Agfa Gevaert Ag Process for producing color photographic images
    DE2102713A1 (en) * 1971-01-21 1972-08-10 Agfa-Gevaert Ag, 5090 Leverkusen Hardening bleach-fix baths
    FR2241095A1 (en) * 1973-08-16 1975-03-14 Eastman Kodak Co
    US4914009A (en) * 1986-06-30 1990-04-03 Fuji Photo Film Co., Ltd. Process for forming direct positive color image comprising the use of bleach accelerators
    DE4034873A1 (en) * 1990-11-02 1992-05-07 Wolfen Filmfab Ag Photographic colour bleaching bath prodn. - by adding accelerator of 3-mercapto-s-triazole to conc soln., for silver halide gelatin emulsion
    US5266121A (en) * 1992-08-12 1993-11-30 Helion Industries, Inc. Method of cleaning photographic processing equipment
    US5476593A (en) * 1994-12-08 1995-12-19 Eastman Kodak Company Method for flushing an undesired precipitate from apparatus surfaces
    US5464727A (en) * 1995-02-08 1995-11-07 Eastman Kodak Company Cleaning of emulsion manufacturing apparatus

    Cited By (2)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    CN113900349A (en) * 2021-10-25 2022-01-07 陕西师范大学 Method for removing silver mirror on surface layer of black and white negative film
    CN113900349B (en) * 2021-10-25 2023-08-18 陕西师范大学 Method for removing silver mirror on surface layer of black-and-white negative film

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