![](/images/new-backgrounds/1232807/23280723x1.webp)
Table
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| KODAK Formula |
| Temperature* |
| Time | Replenisher | Recirculation (R); | |||||
Process Steps |
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| Filtration (F); | ||||
Tank |
| Replenisher |
| °C |
| °F |
| min:sec | 100 ft. (30.5 m) | ||||
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| Turbulation (T) | |||||||
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| of 35 mm Film† | ||||||
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Developer‡ |
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| 36.7 ± | 0.1 | 98.0 | ± | 0.2 | 3:00 | 690 mL | R, F§, & T¶ | |||
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| @125 to 175 L/min | ||||||||||
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Stop ** |
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| 27 ± | 1 | 80 | ± | 2 | :40 | 770 mL | R & F | |||
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| @ 40 to 60 L/min | ||||||||||
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Wash |
| — |
| — | 27 | ± | 3 | 80 | ± | 5 | :40 | 1.2 L†† | None |
Accelerator ‡‡ | ,** |
| 27 ± | 1 | 80 | ± | 2 | :20 | 200 mL | R & F | |||
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| @40 to 60 L/min | ||||||||||
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Persulfate Bleach ‡‡ ,** |
| 27 ± | 1 | 80 | ± | 2 | :40 | 200 mL | R & F§ | ||||
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| @ 40 to 60 L/min | ||||||||||
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Wash |
| — |
| — | 27 | ± | 3 | 80 | ± | 5 | :40 | 1.2 L§§ | None |
Fixer |
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| 27 ± | 1 | 80 | ± | 2 | :40 | ¶¶ | R & F | |||
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| @ 40 to 60 L/min | |
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Wash |
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| — | 27 | ± | 3 | 80 | ± | 5 | 1:00 | 1.2 L§§ | None |
Final Rinse *** |
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| 27 ± | 3 | 80 | ± | 5 | :10 | 400 mL | R & F | |||
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| @ 40 to 60 L/min |
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| Type |
| Temperature |
| RH | Air Flow | Time | ||||
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Dryer |
| Impingement |
| 57°C (135°F) |
| 15% to 25% | 5000ft3/min | 3 to 5 min. | |||||
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| Nonimpingement |
| 43° to 49°C |
| 15% to 25% | 5000ft3/min | 5 to 7 min. | |||||
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| (110° to 120°C) | ||||||||||
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Lubrication |
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| 35 mm |
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| Edgewax |
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| 16 x 18 mm |
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*Celsius temperatures are rounded consistent with
† For 16 mm film, use
‡ Maintain close control of developer time and temperature, since small deviations can lead to severe contrast mismatch. Use an accurate thermometer for checking the temperature controller variability. The temperature should be uniform throughout the developer tank.
§Use polypropylene, fiberglass, or bleached cotton as a filter medium in the developer. Viscose rayon is not recommended for the developer or bleaches because of undesirable photographic effects.
¶ Design developer racks with submerged rollers and
**Install an exhaust over the stop tank, since developer carried over into the stop generates sulfur dioxide. Install an exhaust over the accelerator tank to eliminate odors. Install an exhaust over the persulfate bleach tanks to eliminate corrosion from chlorine vapors. The exhaust system should produce an
air flow of 175 ft3/min (5 m3/min) for every square foot (0.09m2) of solution surface, and provide 50 to 75 ft/min (15 to 23 m/min) control velocity over the surface of the tank.
†† The stop wash rates given in this table assume the use of
‡‡Reconstitute and reuse persulfate bleach
§§The wash rate given in this table assumes that the final wash and bleach wash are composed of three
¶¶Fixer replenisher requirements vary with silver recovery equipment, method, and operating conditions. If provision is made fo r continuous electrolytic desilvering for the recirculated fixer, the silver concentration should be maintained between 0.5 and 1 g/L. See Module 5, Chemical Recovery Procedures, for details. The fixer and replenisher must be kept separate from other processes. Savings from reconstituting desilvered fixer overflow for use as replenisher are possible.
***Processing the print film does not require a formaldehyde stabilizer, therefore you may use Final Rinse,
Process |