Bleach regenerator composition and its use to process reversal color photographic elements

Abstract: A ferric-EDTA bleach regenerator composition can be mixed with bleach overflow to provide a bleach replenisher for reversal color silver halide photographic processes. The bleach regenerator composition has a critically controlled pH between 6.0 and 6.5, and comprises a total bromide ion concentration of at least 210 g/l, and ferric ion in an amount of at least 50 g/l. At least 50% of the bleach overflow and the bleach regenerator composition are mixed in at least a 1:1 volume ratio. After pH adjustment to from 5.4 to 5.6, the pH adjusted replenisher is supplied to the bleach tank for use in the process.

Description: This invention relates in general to color photography and in particular to methods and compositions useful in the processing of color reversal photographic elements. More particularly, this invention relates to a bleach regenerator composition, and its use in the processing of the noted elements. Multicolor, multilayer photographic elements are well known in the art. Such materials generally have three different selectively sensitized silver halide emulsion layers coated on one side of a single support. Each layer has components useful for forming a particular color in an image. Typically, they utilize color forming couplers that form yellow, magenta and cyan dyes in the sensitized layers during processing. After color development, it is necessary to remove the silver image that is formed coincident with the dye image. This can be done by oxidizing the silver using a suitable oxidizing agent, commonly referred to as a bleaching agent, followed by dissolving the silver halide so formed using what is known as a fixing agent. A commercially important process intended for use with color reversal photographic elements that contain color couplers in the emulsion layers, or layers contiguous thereto, uses the following sequence of processing steps: first developing, washing, reversal bath, color developing, bleaching, fixing, washing and stabilizing. In the past, in continuous processing methods, including processing of reversal color materials, the various processing solutions have been discarded after use. However, more recently, used processing solutions have been collected and reused, at least in part because of the environmental problems the waste solutions create, as well as the high costs in collection and discard of the solutions. Thus, used solutions have been reused by adding them to the processing baths as "replenishers" to the various solutions. Considerable efforts are being carried out in the industry to find ways to regenerate the components of the waste solutions so they can be reused as replenishers, further reducing waste streams. For example, a bleach replenishing composition is added to the bleach tank to keep the necessary components at the appropriate levels. This bleach replenisher can be composed of, in part, bleach composition overflow. As environmental needs increase in various countries, the industry is striving to find ways to further reduce photoprocessing effluent from the various processing baths. Thus, efforts have been made to regenerate the bleaching solution overflow and to supply the regenerated replenisher solution to the bleach tank as the replenishment solution. One known bleach regenerator solution for reversal color processes is sold by Tetenal of Germany (sold as Tetenal Bleachbath E6/E6AR BL-RCY), which has a pH of 7, and contains a relatively high bromide ion concentration (approximately 190-210 g/l). There is also a desire in the industry to use a more concentrated bleach regenerator so more bleaching solution overflow can be utilized to make the bleach replenisher, thereby reducing effluent even further. The commercial product available from Tetenal, however, has limited shelf life stability at its "neutral" pH. It was considered that its pH might be lowered to increase stability, but when this was done, its solubility was decreased and precipitation resulted after several days. Another problem with the commercial Tetenal regenerator solution is that when acid is added to it to lower its pH to the level needed for converting it to a regenerated replenisher, the bleaching capacity of the resultant bleach tank solution is degraded. There is a need therefore for a more stable bleach regenerator composition that can be used in highly concentrated form to provide a regenerated bleach replenisher at lower pH. The problems noted above have been overcome using a method for processing a reversal color silver halide photographic element comprising: A) bleaching an imagewise exposed, color developed reversal color silver halide photographic element in a bleaching tank with a bleaching composition comprising a complex of ferric ethylenediaminetetraacetic acid as the bleaching agent, B) supplying a bleach replenisher to the bleaching tank to result in an overflow of used bleaching composition from the bleaching tank, C) mixing at least 50% of the overflow, in at least a 1:1 volume ratio, with a bleach regenerator composition to obtain a regenerated bleach replenisher, the bleach regenerator composition having a pH of from 6.0 to 6.5, and comprising a total bromide ion concentration of at least 210 g/l, and complex of ferric ion and ethylenediaminetetraacetic acid, the ferric ion being present in an amount of at least 50 g/l, D) adjusting the pH of the regenerated bleach replenisher prepared in step C to from 5.4 to 5.6, and E) replenishing the bleaching composition of step A in the bleaching tank with the pH adjusted regenerated bleach replenisher prepared in step D, using a bleach replenishment rate of less than or equal to 215 ml/m 2 . This invention also provides a bleach regenerator composition characterized as having a pH of from 6.0 to 6.5, and comprising a total bromide concentration of at least 210 g/l, and a complex of ferric ion and ethylenediaminetetraacetic acid, the ferric ion being present in an amount of at least 50 g/l. The present invention effectively provides a bleach regenerator composition for processing reversal color silver halide photographic materials. The bleach regenerator composition is more stable and stays in solution even at lower pH for extended periods of time. The composition is highly concentrated, for example, in the ferric ion concentration, so that more bleach overflow can be used to form the bleach replenisher. These advantages are achieved by using a bleach regenerator composition at considerably lower pH, that is, 6.0-6.5, and thus stability is improved. However, in order to maximize the concentration of the components, the level of bromide salt and hydrobromic acid have been adjusted to provide a reformulated and improved composition. A wide variety of reversal color photographic elements can be used in the practice of the present invention. A detailed description of such materials is found, for example, in Research Disclosure , publication 36544, pages 501-541 (September, 1994). This reference will be referred to hereinafter as " Research Disclosure ". More details such elements are provided herein below. Reversal color photographic elements utilized in the practice of this invention are typically comprised of a support having on one side thereof a plurality of photosensitive silver halide emulsion layers. The photosensitive layers can contain any of the conventional silver halides as the photosensitive material, for example, silver chloride, silver bromide, silver bromoiodide, silver chlorobromide, silver chloroiodide, silver chlorobromoiodide, and mixtures thereof. Useful support materials include cellulose acetate film, polyvinylacetal film, polycarbonate film, polystyrene film, polyethylene terephthalate film, and the like. The silver halide is dispersed within a suitable hydrophilic colloid such as gelatin or derivatives thereof. The silver halide emulsion layers can contain a variety of well-known addenda, including but not limited to, chemical sensitizers, development modifiers and antifoggants. As explained above, a well-known color reversal process of the prior art utilizes a first developer, a reversal bath, a color developer, a conditioning solution, a bleach bath, a fixing bath and a stabilizer bath. Alternatively, the stabilizer bath can be replaced with a typical wash or rinse solution, and a "prebleach" or "conditioner" bath is used for stabilizing the color image after color development and prior to bleaching. The components that are useful in each of such baths are well known in the photographic art. The improved process of this invention can utilize the same baths. The first developer generally contains a black-and-white developing agent or a mixture thereof. Useful developing agents include, but are not limited to, dihydroxybenzene developing agents (such as hydroquinone), 3-pyrazolidone developing agents (such as 1-phenyl-3-pyrazolidone), and aminophenol developing agents (such as paraaminophenol). In addition to the developing agent, the first developer typically contains other agents such as preservatives, sequestering agents, restrainers, antifoggants, buffers and silver halide solvents. The reversal bath generally contains a nucleating agent, such as a boron compound or a chelated stannous salt (such as stannous chloride) that functions as a reducing agent, as well as antioxidants, buffers, fungicides and sequestering agents. In addition to an aromatic primary amino color developing agent, the color developing bath typically contains sequestering agents, buffering agents, preservatives, antioxidants, competing couplers and silver halide solvents. Particularly useful aromatic primary amino color developing agents are the p -phenylenediamines and especially the N,N-dialkyl- p -phenylenediamines in which the alkyl groups or the aromatic nucleus can be substituted or unsubstituted. Examples of useful p -phenylenediamine color developing agents include, but are not limited to, N,N-diethyl- p -phenylenediamine monohydrochloride, 4-N,N-diethyl-2-methylphenylenediamine monohydrochloride, 4-(N-ethyl-N-2-methanesulfonylaminoethyl)-2-methylphenylenediamine sesquisulfate monohydrate, 4-(N-ethyl-N-2-hydroxyethyl)-2-methyl-phenylenediamine sulfate, 4-N,N-diethyl-2,2'-methanesulfonylaminoethylphenylenediamine hydrochloride, and others readily apparent to a skilled worker in the art. The essential component of the bleaching bath is a bleaching agent that converts metallic silver to silver ions. Other common components of the bleaching bath include halides, sequestering agents and corrosion inhibitors. One or more ammonium or alkali metal salts of a ferric complex of ethylenediaminetetraacetic acid are useful as bleaching agents in this invention. The fixing bath converts all silver halide into soluble silver complexes that diffuse out of the emulsion layers. Fixing bath retained within the layers of the photographic element is removed in a subsequent water washing step. Thiosulfates, including ammonium thiosulfate and alkali metal thiosulfates (such as sodium thiosulfate and potassium thiosulfate), are particularly useful as fixing agents. Other components of the fixing bath include preservatives and sequestering agents. A wide variety of different color reversal processes are well known in the art. For example, a single color developing step can be used when the coupling agents are incorporated in the photographic element or three separate color developing steps can be used in which coupling agents are included in the developing solutions. The reversal step can be carried out by use of a reversal bath, by a reexposure step, or by incorporating a fogging agent in the color developing bath. In order to provide shorter processing times, bleaching and fixing can be combined in a single step (known as a bleach-fixing step). Stabilization solutions are also known in the art for use in reversal photoprocessing methods. Such solutions generally include formaldehyde or an equivalent material to stabilize magenta dye image. Further details of such solutions are provided, for example, in US-A-4,786,583. Alternatively and preferably, stabilization is achieved by using a prebleach or conditioning solution after color development and prior to bleaching. The various details of such solutions and their use are provided, for example, in US-A-4,921,779, US-A-4,975,356, US-A-5,037,725, and US-A-5,334,493. Other optional features of useful conditioning solutions are secondary amines. The bleaching composition used in this invention comprises a complex of ferric ion and ethylenediaminetetraacetic acid in a suitable concentration. The amount of iron(III) is generally from 50 to 58 g/l. One or more salts of the complex can be used if desired. The bleaching composition is supplied to the bleach tank in a suitable rate to result in an overflow of used bleaching solution from the bleaching tank. Generally, the rate of supply is less than or equal to 215 ml/m 2 , and preferably from 140 to 215 ml/m 2 . At least 50%, preferably from 50 to 80%, and more preferably from 50 to 75%, of the bleaching composition overflow is mixed with the bleach regenerator composition to obtain a regenerated bleach replenisher. The mixing is carried out in at least a 1:1 volume ratio of bleaching composition overflow to bleach regenerator composition, and up to 9:1. Preferably, the volume ratio of mixing is from 1:1 to 3:1. After mixing, the pH of the regenerated bleach replenisher is adjusted downward to from 5.4 to 5.6 by adding a suitable amount of an organic or inorganic acid, such as acetic acid, succinic acid, maleic acid, tartaric acid, malonic acid, or nitric acid. Acetic acid is preferred. The amount of acid to be added could be readily determined by routine experimentation, depending upon the pH of the regenerated bleach replenisher and the particular acid used. For acetic acid, the amount added is generally from 10 to 20 ml/l. One advantage of this invention is that less acid needs to be added to the regenerated bleach replenisher than to conventional regenerator solutions. The pH adjusted regenerated bleach replenisher is then added to the bleaching tank as the "bleach replenisher" at a bleach replenishment rate of less than or equal to 215 ml/m 2 , and preferably at from 140 to 215 ml/m 2 . The bleach regenerator composition used in the method of this invention has a pH of from 6.0 to 6.5 (preferably from 6.0 to 6.2). It includes the bleaching agent, a ferric ion complex of ethylenediaminetetraacetic acid in an amount to provide ferric ion in an amount of at least 50 g/l, and preferably at from 50 to 58 g/l. Ferric ion can be supplied for the complex as a suitable ferric salt or oxide, such as ferric nitrate, ferric sulfate, ferric oxide or ferric bromide. Ferric oxide or ferric nitrate is preferred. The complex can be provided as an ammonium or alkali metal salt, as well as the free acid. Also included in the bleach regenerator composition are one or more sources of bromide ion such that the total bromide ion is present in an amount of at least 210 g/l, preferably at from 215 to 240 g/l, and most preferably at from 220 to 240 g/l. Preferably, total bromide ion is provided by a combination of hydrobromic acid and a bromide salt (such as sodium bromide, potassium bromide, ammonium bromide or lithium bromide). More preferably, at least 80%, more preferably from 80 to 97%, of the total bromide ion is provided from the bromide salt, and the remainder from the hydrobromic acid. Ammonium bromide is most preferred. One or more corrosion inhibitors can also be included in the bleach regenerator composition if desired at suitable concentrations. Preferably, such corrosion inhibitors include, but are not limited to, the potassium salts of nitrate, silicate, chromate and phosphate. Hexamethylenetetraamine and benzotriazole can also be used. Potassium nitrate is preferred. A preferred embodiment of this invention is a bleach regenerator composition having a pH of from 6.0 to 6.2, and comprising: a) a total bromide ion concentration of from 220 to 240 g/l provided by a combination of hydrobromic acid and a bromide salt, the amount from the bromide salt being from 80 to 97% of the total bromide ion, b) a complex of ferric ion and ethylenediaminetetraacetic acid, the ferric ion being present in an amount of from 50 to 58 g/l, and c) a corrosion inhibitor. The photographic elements processed in the practice of this invention can be single or multilayer color elements. Multilayer color elements typically contain dye image-forming units sensitive to each of the three primary regions of the visible spectrum. Each unit can be comprised of a single emulsion layer or multiple emulsion layers sensitive to a given region of the spectrum. The layers of the element can be arranged in any of the various orders known in the art. In an alternative format, the emulsions sensitive to each of the three primary regions of the spectrum can be disposed as a single segmented layer. The elements can also contain other conventional layers such as filter layers, interlayers, subbing layers, overcoats and other layers readily apparent to one skilled in the art. A magnetic backing can be used as well as conventional supports. Considerable details of the element structure and components, and suitable methods of processing various types of elements are described in Research Disclosure , noted above. All types of emulsions can be used in the elements, including but not limited to, thin tabular grain emulsions, and either positive-working or negative-working emulsions. The present invention is particularly useful to process imagewise exposed and developed photographic elements containing arylpyrazolone type magenta dye forming color couplers. Such color couplers are well known in the art. One such compound is described in US-A-5,037,725. Useful cyan dye and yellow dye forming couplers that can be incorporated into such elements are also well known. The elements are typically exposed to suitable radiation to form a latent image and then processed as described above to form a visible dye image. The bleaching step described above is generally carried out for from 4 to 8 minutes, but longer times can be used if desired. Preferably, the bleaching time is 6 minutes. The temperature at which bleaching is carried out is generally above room temperature, for example from 30 to 40 °C. Processing according to the present invention can be carried out using conventional deep tanks holding processing solutions. Alternatively, it can be carried out using what is known in the art as "low volume thin tank" processing systems having either vertical rack and tank or horizontal automatic tray designs. Such processing methods and equipment are described, for example, in US-A-5,436,118 and publications cited therein. The following examples are provided for illustrative purposes only and are not intended to be limiting in any way. Unless otherwise indicated, all percentages are by volume. Example 1: Preferred Bleach Regenerator Composition A preferred bleach regenerator composition of this invention was prepared by mixing the following in water (added to make 1 liter total): commercially available 1.56 molar ammonium ferric-ethylenediaminetetraacetic acid (788 g), hydrobromic acid (61.5 g), ammonium bromide (243.9 g) and potassium nitrate (67 g). The final pH was 6.0-6.2. Example 2: Preferred Regenerated Bleach Replenisher Composition & Comparison The bleach regenerator composition of Example 1 was mixed with seasoned conventional color reversal bleach composition overflow comprising 1.56 molar ammonium ferric-ethylenediaminetetraacetic acid bleaching agent (277 g/l), bromide ion from various salts (73.8 g/l), and potassium nitrate (25 g/l). The volume ratio of bleach composition (which is comparable to bleach overflow) to bleach regenerator composition was 1:1. The resulting regenerated bleach replenisher had a pH of 5.95-6.1. The pH was then adjusted downward to 5.4-5.6 by adding acetic acid (18 ml/l) to provide a pH adjusted regenerated bleach replenisher that can be directly added to a bleach bath to process reversal color silver halide photographic materials. As noted above, the amount of acetic acid needed to adjust the pH of the regenerated bleach replenisher was only 18 ml/l. However, when the commercially available Tetenal Bleachbath E6/E6AR BLRCY regenerator solution was used in a similar fashion, it was necessary to add acetic acid at 30 ml/l in order to obtain the desired pH. Thus, clearly the present invention allows one to reduce the amount of acid in preparing a bleach replenisher, and this acid reduction provides advantages as noted above. Example 3: Processing Reversal Color Photographic Elements The regenerated bleach replenisher compositions of this invention were evaluated in otherwise conventional reversal color photographic processing. The invention was used to process samples of a conventional color reversal photographic films (available from Eastman Kodak Company) using the following processing protocol. This film contained a conventional 1-aryl-5-pyrazolone magenta color coupler in one of the emulsion layers. Processing Protocol: 6 minutes First Development 2 minutes Water wash 2 minutes Reversal bath 6 minutes Color development 2 minutes Prebleach 6 minutes Bleaching 4 minutes Fixing 4 minutes Water wash 30 seconds Final wash 20 minutes Drying The method of this invention was carried out by taking at least 50% of the bleach bath overflow and mixing it (at a 1:1 volume ratio) with the bleach regenerator composition of Example 1. This mixing was carried out for 3 minutes at 20-25 °C in a separate vessel. The mixture pH of 5.9-6.1 was then adjusted downward by adding acetic acid as described in Example 2, and the adjusted mixture was then added to the bleach bath as a replenisher for the process. This method was carried out for at least 4 bleach tank turn-overs, or for at least 330 m 2 of processed reversal color photographic film. The results of processing were highly acceptable. That is, use of the noted regenerated bleach composition provided highly acceptable processing of the film. Examples 4-6: Effects of pH in Bleach Regenerator Composition Experiments were carried out to show the critical importance of the bleach regenerator composition having a pH of from 6.0 to 6.5. Several regenerator compositions like that described in Example 1 above were subjected to keeping tests to see if crystallization or precipitation would occur. The various compositions had components like Example 1 and various pH values as shown in Table I below. The results of the keeping tests are shown in Table I for the various compositions. Column 1 lists the keeping temperatures (from -18 to +21 °C) at which the compositions were stored for 14 days. Column 2 shows when the crystallization results were observed (at room temperature) after the compositions were removed from the keeping environment, that is "Observation Time After Removal". Thus, samples of each composition were observed immediately ("0" time), 24 hours, and 11 days after they were removed from the keeping environment. Crystals of ammonium ferric ethylenediaminetetraacetic acid complex were measured by visual inspection and identified by Fourier Transform Infrared (FTIR) spectroscopy. The results indicate that best time and temperature stability for the composition is achieved when the pH is at least 6.0. It is noted that Control C, while being stable at a pH above 6.5, is undesirable because at such high pH, unacceptably high amounts of acid must be added to the regenerated bleach replenisher to lower the pH to an acceptable level before it can be added to the bleach bath as replenisher. In addition, several bleaching compositions were subjected to high temperature (49 °C) keeping for 12 days. Examples 4 and 6 were compared to three "Control" bleaching compositions outside this invention, including Control C identified above. Control D was a commercial Process E-6 (reversal) Bleach Replenisher containing ferric ethylenediaminetetraacetic acid bleaching agent and having pH 5.4. Control E was a commercial highly concentrated (1.56 mol/l) ammonium ferric ethylenediaminetetraacetic acid, KODAK BL-1, having pH 7.0. The results of ferrous ion build-up (g/l) after keeping are listed in Table II below. It was observed that the pH dropped in all compositions during the high temperature keeping test, but subsequent freezing of the compositions did not cause precipitation. Composition pH Ferrous Ion Buildup (g/l) Control D 5.4 7 Example 4 6.0 33 Example 6 6.5 37 Control C 6.9 40 Control E 7.0 60 To determine if the change in pH after keeping might diminish bleaching performance of the regenerator compositions, Examples 4 and 6 and Control C were formulated into working strength bleaching solutions, and were then used to bleach three different commercially available reversal color films: KODAK EKTACHROME™ 400 HC Film, KODAK EKTACHROME™ ELITE™ 100 Film and KODAK EKTACHROME™ 64 Professional Film. A solution made from a pH 6.5 concentrate, which had been kept at room temperature, was used as the "Standard" solution. All compositions were brought to the same total iron level and then aerated to oxidize any ferrous ion to ferric ion. Once this was completed, the compositions were all pH adjusted to the standard bleaching pH of 5.8 Table III below lists the "bleach clear times" for each regenerator composition tested. "Bleach clear time" refers to the time at which all metallic silver has been converted to silver halide for subsequent dissolution and removal in the following fixing step. The results indicate that a regenerator composition pH of 6.0-6.5 is desired for improved composition keeping. Composition Bleach Clear Time (seconds) Standard 252 Example 4 313 Example 6 342 Control C 337 Example 7: Effect of Bromide Level in Bleach Regenerator Composition Experiments were also carried out to show the effect of bromide ion concentration in the bleach regenerator composition of this invention. A 2 4 factorial experiment with optimized "aims" was carried out around the chemical ingredients of a conventional Process E-6 bleaching solution. One of those components is bromide ion. The level of bromide ion was varied while all other components were kept at optimized levels for processing two different commercially available color reversal photographic films, and the bleach "clear time" (seconds to convert all silver metal to silver halide) was determined. The optimized or "aim" level for bromide ion in the bleaching solution was considered to be 73.4 g/l. The following Table IV lists the data obtained. Bromide Ion (g/l) Predicted Clear Bleaching Time (seconds Average Δ Clear Time (seconds) Film #1 Film #2 65.8 301 309 44 73.4 (aim) 273 282 81.0 259 263 As one can see from these data, the average reduction in "clear time" during bleaching for processing the two films from varying the bromide ion level, was 44 seconds. This was surprising to us. It had been previously thought that because the bromide ion in conventional replenisher is relatively high (145-150 g/l), that the amount of bromide ion "used" during bleaching would not have a significant impact on the rate of bleaching (and thus, the bleaching "clear time"). These experiments proved otherwise and showed the significant potential magnitude of the impact from increased bromide ion concentration. We discovered that with reuse or regeneration of the bleaching solution (in which case, the bromide ion is "used up" repeatedly and tank concentration would drop below levels seen in conventional replenishment), additional bromide ion must be added to compensate for the usage, as well as for the deterioration in bleaching rate (and thus, bleach "clear time") due to additional build-up of carryover products. Bleach replenisher provides three benefits to the tank bleaching solution: 1) dilution of chemicals carried in and undesirable chemicals produced in chemical reactions, 2) addition of chemicals, such as bromide ion, to make up for those used in chemical reactions necessary for bleaching, and 3) make up for chemicals that are diluted by carryover or carried out into the next solution (that is the fixing solution). The conventional Tetenal Process E-6 bleach regenerator has bromide ion levels which account only for the first and third benefits noted above. We have found that this is inadequate, and that the level of bromide ion in the bleach regenerator must also be adjusted for bromide ion used up in the bleaching reaction (approximately 14-18 g/l of replenisher when processing elements containing 4.3-5.4 g silver/m 2) . Thus, we determined that the level of bromide ion needed to be increased in the regenerator composition that is used to provide a regenerated bleach replenisher, and the present invention reflects that fact.

Claims: A bleach regenerator composition characterized as having a pH of from 6.0 to 6.5, and comprising a total bromide ion concentration of at least 210 g/l, and a complex of ferric ion and ethylenediaminetetraacetic acid, the ferric ion being present in an amount of at least 50 g/l. The composition as claimed in claim 1 having a pH of from 6.0 to 6.2. The composition as claimed in either of claims 1 and 2 having a total bromide ion concentration of from 215 to 240 g/l. The composition as claimed in any of claims 1 to 3 wherein the total bromide ion is provided by a combination of a hydrobromic acid and a bromide salt, the bromide ion provided by the bromide salt being at least 80% of the total bromide ion. The composition as claimed in any of claims 1 to 4 wherein the ferric ion is present in an amount of from 50 to 58 g/l. The composition as claimed in any of claims 1 to 5 further comprising a corrosion inhibitor. A method for processing a reversal color silver halide photographic element comprising: A) bleaching an imagewise exposed, color developed reversal color silver halide photographic element in a bleaching tank with a bleaching composition comprising a complex of ferric ethylenediaminetetraacetic acid as the bleaching agent, B) supplying a bleach replenisher to the bleaching tank to result in an overflow of used bleaching composition from the bleaching tank, C) mixing at least 50% of the overflow, in at least a 1:1 volume ratio, with the bleach regenerator composition as claimed in any of claims 1 to 6 to obtain a regenerated bleach replenisher, D) adjusting the pH of the regenerated bleach replenisher prepared in step C to from 5.4 to 5.6, and E) replenishing the bleaching composition of step A in the bleaching tank with the pH adjusted regenerated bleach replenisher prepared in step D, using a bleach replenishment rate of less than or equal to 215 ml/m 2 . The method as claimed in claim 7 wherein the bleach replenishment rate is from 140 to 215 ml/m 2 . The method as claimed in either of claims 7 or 8 wherein from 50 to 80% of the bleach tank overflow is mixed with the bleach regenerator composition in step C. The method as claimed in any of claims 7 to 9 wherein the volume ratio of the bleach tank overflow to the bleach regenerator composition is up to 9:1. The use of the bleach regenerator composition claimed in any of claims 1 to 6 for the processing of reversal color silver halide photographic materials.

Inventors: BUONGIORNE JEAN MARIE, CRAVER MARY ELLEN, HAIGHT MICHAEL JOHN, BUONGIORNE, JEAN MARIE, CRAVER, MARY ELLEN, HAIGHT, MICHAEL JOHN
Applicants: EASTMAN KODAK CO, EASTMAN KODAK COMPANY
Application year: 1996
Main classification: G03C7
IPC codes: G03C5, G03C7