Journal of the Society of Motion Picture and Television Engineers (1950-1954)

Record Details:

Something wrong or inaccurate about this page? Let us Know!

Thanks for helping us continually improve the quality of the Lantern search engine for all of our users! We have millions of scanned pages, so user reports are incredibly helpful for us to identify places where we can improve and update the metadata.

Please describe the issue below, and click "Submit" to send your comments to our team! If you'd prefer, you can also send us an email to mhdl@commarts.wisc.edu with your comments.




We use Optical Character Recognition (OCR) during our scanning and processing workflow to make the content of each page searchable. You can view the automatically generated text below as well as copy and paste individual pieces of text to quote in your own work.

Text recognition is never 100% accurate. Many parts of the scanned page may not be reflected in the OCR text output, including: images, page layout, certain fonts or handwriting.

WARM COMPRESSED AIR CARBON DIOXIDE (OPTIONAL) Q I 1 ELECTROLYSIS CELL FIXING TANK SPRAY WASH TANK DRYER Fig. 3. Schematic representation of vanadium processing machine: 1, lead cathode; 2, porous cup; 3, carbon anode; 4, vent:anode compartment; 5, vent:cathode compartment; 6, column of orifices through which developer is forced to give immersed-jet agitation; 7, drive and squeegee. Arrows in developer recirculation system show the direction of solution flow. The electrolysis cell, the developing tank, and the drying cabinet are of Plexiglas, while all other parts that come in contact with solutions are of Type 316 stainless steel. heat-exchange system back to the immersed jets of the developing tank. The electrolytic cell in the system serves as a novel method of maintaining developer activity. Oxidized vanadium formed by the development process and aeration is electrolytically reduced in the cell and the composition of the developer remains essentially constant. The only loss is represented by the amount of solution carried out on the film, and with proper squeegeeing, this may be kept at a low level. Runs have been made where carry-out rates of approximately 0.3 ml/ft of 35mm film have prevailed. After development, the film immediately passes through a spray water rinse which acts as a stop bath. From this point, the film is conventionally fixed, washed and dried, except that an ammonium hypo fixer, spray wash and warm, forced-air current are employed, so that the rate of these processing steps will be consistent with the developing rate. Figures 4 and 5 show the experimental machine with which the vanadium development tests were made. Processing Procedure Using the optimum vanadium developer formula, Eastman Fine Grain Release Positive Film, Type 5302, is developed in 15 to 20 sec at 60 F on the experimental machine with a film speed of about 6 ft/min. The developing section is charged with a solution prepared in an external electrolytic cell, the electrolysis being performed external to the machine primarily to save time. Continuous electrolytic regeneration of the vanadium developer during a processing run requires relatively little current and consequently the electrolytic Rasch and Crab tree: Development by Vanadous Ion