Sometimes the temperature of the cold water supply may be higher than required by theprocessor. In this situation, it is necessary to cool the water before pip<strong>in</strong>g it to the processor.This is the basic pattern of the water system of automated processors; the details of the systemmay vary slightly, however.Recirculation SystemsRecirculation of the fixer and developer solutions performs the triple functions of uniformly mix<strong>in</strong>gthe process<strong>in</strong>g and replenisher solution, ma<strong>in</strong>ta<strong>in</strong><strong>in</strong>g them at constant temperatures, and keep<strong>in</strong>gthoroughly mixed and agitated solutions <strong>in</strong> contact with the film.The solutions are pumped from the processor tanks, passed through devices to regulatetemperature, and returned to the tanks under pressure. This pressure forces the solutions upwardand downward, <strong>in</strong>side, and around the transport system assemblies. As a result of the vigorousflow <strong>in</strong> the process<strong>in</strong>g tanks, the solutions are thoroughly mixed and agitated and the filmsmov<strong>in</strong>g through the tanks are constantly bathed <strong>in</strong> fresh solutions.Replenishment SystemsAccurate replenishment of the developer and fixer solutions is even more important <strong>in</strong> automatedprocess<strong>in</strong>g than <strong>in</strong> manual process<strong>in</strong>g. In both techniques, accurate replenishment is essential toproper process<strong>in</strong>g of the film and to long life of the process<strong>in</strong>g solutions; but, if the solutions arenot properly replenished <strong>in</strong> an automated processor, the film may swell too much and becomeslippery, with the result that it might get stuck <strong>in</strong> the processor.When a film is fed <strong>in</strong>to the processor, pumps are activated, which pump replenisher from storagetanks to the process<strong>in</strong>g tanks. As soon as the film has passed the entrance assembly, the pumpsstop--replenisher is added only dur<strong>in</strong>g the time required for a sheet of film to pass through theentrance assembly. The amount of replenisher added is thus related to the size of the sheet offilm. The newly added replenisher is blended with the processor solutions by the recirculationpumps. Excess process<strong>in</strong>g solutions flow over a weir at the top of the tanks <strong>in</strong>to the dra<strong>in</strong>.Different types of x-ray films require different quantities of process<strong>in</strong>g chemicals. It is, therefore,important that the solutions be replenished at the rate proper for the type or types of film be<strong>in</strong>gprocessed and the average density of the radiographs.Replenishment rates must be measured accurately and checked periodically. Overreplenishmentof the developer is likely to result <strong>in</strong> lower contrast; slight underreplenishment results <strong>in</strong> ga<strong>in</strong> ofspeed and contrast, but severe underreplenishment results <strong>in</strong> a loss of both. Severeunderreplenishment of developer can cause not only loss of density and contrast but also failureof the film to transport at any po<strong>in</strong>t <strong>in</strong> the transport system. Overreplenishment of the fixer doesnot affect good operation, but is wasteful. However, underreplenishment results <strong>in</strong> poor fixation,<strong>in</strong>sufficient harden<strong>in</strong>g, <strong>in</strong>adequate wash<strong>in</strong>g, and possible failure of the film to be transported <strong>in</strong>the fixer rack or at any po<strong>in</strong>t beyond.Dryer SystemRapid dry<strong>in</strong>g of the processed radiograph depends on proper condition<strong>in</strong>g of the film <strong>in</strong> theprocess<strong>in</strong>g solutions, effective removal of surface moisture by the squeegee rollers, and a goodsupply of warm air strik<strong>in</strong>g both surfaces of the radiograph.Heated air is supplied to the dryer section by a blower. Part of the air is recirculated; the rest isvented to prevent buildup of excessive humidity <strong>in</strong> the dryer. Fresh air is drawn <strong>in</strong>to the system toreplace that which is vented.<strong>Radiography</strong> <strong>in</strong> <strong>Modern</strong> <strong>Industry</strong> 116
Rapid Access to Processed RadiographsApproximately twelve or fourteen m<strong>in</strong>utes after exposed films are fed <strong>in</strong>to the unit, they emergeprocessed, washed, dried, and ready for <strong>in</strong>terpretation. Conservatively, these operations takeapproximately 1 hour <strong>in</strong> hand process<strong>in</strong>g. Thus, with a sav<strong>in</strong>g of at least 45 m<strong>in</strong>utes <strong>in</strong> process<strong>in</strong>gtime, the hold<strong>in</strong>g time for parts be<strong>in</strong>g radiographed is greatly reduced. It follows that more workcan be scheduled for a given period because of the speed of process<strong>in</strong>g and the consequentreduction <strong>in</strong> space required for hold<strong>in</strong>g materials until the radiographs are ready for check<strong>in</strong>g.Uniformity of RadiographsAutomated process<strong>in</strong>g is very closely controlled time-temperature process<strong>in</strong>g. This, comb<strong>in</strong>edwith accurate automatic replenishment of solutions, produces day-after-day uniformity ofradiographs rarely achieved <strong>in</strong> hand process<strong>in</strong>g. It permits the sett<strong>in</strong>g up of exposure techniquesthat can be used with the knowledge that the films will receive optimum process<strong>in</strong>g and be freefrom process<strong>in</strong>g artifacts. Process<strong>in</strong>g variables are virtually elim<strong>in</strong>ated.Small Space RequirementsAutomated processors require only about 10 square feet of floor space. The size of theprocess<strong>in</strong>g room can be reduced because hand tanks and dry<strong>in</strong>g facilities are not needed. A filmload<strong>in</strong>g and unload<strong>in</strong>g bench, film storage facilities, plus a small open area <strong>in</strong> front of theprocessor feed tray are all the space required. The processor, <strong>in</strong> effect, releases valuable floorspace for other plant activities. If the work load <strong>in</strong>creases to a po<strong>in</strong>t where more processors areneeded, they can be added with m<strong>in</strong>imal additional space requirements. Many plants with widelyseparated exposure areas have found that dispersed process<strong>in</strong>g facilities us<strong>in</strong>g two or moreprocessors greatly <strong>in</strong>crease the efficiency of operations.Chemistry of Automated Process<strong>in</strong>gAutomated process<strong>in</strong>g is not just a mechanization of hand process<strong>in</strong>g, but a system depend<strong>in</strong>gon the <strong>in</strong>terrelation of mechanics, chemicals, and film. A special chemical system is thereforerequired to meet the particular need of automated process<strong>in</strong>g.When, <strong>in</strong> manual process<strong>in</strong>g, a sheet of x-ray film is immersed <strong>in</strong> developer solution, the exposedsilver halide gra<strong>in</strong>s are converted to metallic silver, but, at the same time, the emulsion layerswells and softens. The fixer solution removes the underdeveloped silver halide gra<strong>in</strong>s andshr<strong>in</strong>ks and hardens the emulsion layer. Wash<strong>in</strong>g removes the last traces of process<strong>in</strong>gchemicals and swells the film slightly. Dry<strong>in</strong>g further hardens and shr<strong>in</strong>ks the emulsion.Therefore, the emulsion changes <strong>in</strong> thickness and <strong>in</strong> hardness as the film is moved from one stepto the next <strong>in</strong> process<strong>in</strong>g. In manual process<strong>in</strong>g, these variations are of no importance becausethe films are supported <strong>in</strong>dependently and do not come <strong>in</strong> contact with other films or any othersurfaces.Automated process<strong>in</strong>g, however, places an additional set of demands on the process<strong>in</strong>gchemicals. Besides develop<strong>in</strong>g and fix<strong>in</strong>g the image very quickly, the process<strong>in</strong>g chemicals mustprevent the emulsion from swell<strong>in</strong>g or becom<strong>in</strong>g either slippery, soft, or sticky. Further, they mustprepare the processed film to be washed and dried rapidly.In automated processors, if a film becomes slippery, it could slow down <strong>in</strong> the transport system,so that films follow<strong>in</strong>g it could catch up and overlap. Or it might become too sticky to pass comepo<strong>in</strong>t and get stuck or even wrap around a roller. If the emulsion becomes too soft it could bedamaged by the rollers. These occurrences, of course, cannot be tolerated. Therefore,process<strong>in</strong>g solutions used <strong>in</strong> automated processors must be formulated to control, with<strong>in</strong> narrowlimits, the physical properties of the film. Consequently, the mix<strong>in</strong>g <strong>in</strong>structions with thesechemicals must be followed exactly.<strong>Radiography</strong> <strong>in</strong> <strong>Modern</strong> <strong>Industry</strong> 117
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RadiographyinModernIndustry
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RadiographyinModernIndustryFOURTH E
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ContentsIntroduction...............
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Chapter 1: The Radiographic Process
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Intensifying ScreensX-ray and other
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makes it a very suitable material f
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Figure 6: Typical voltage waveforms
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Table I - Typical X-ray Machines an
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The wavelengths (or energies of rad
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Table III - Industrial Gamma-Ray So
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1. The source of light should be sm
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B and H in the Figure 13 show the e
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Figure 14: Geometric construction f
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Figure 17: Pinhole pictures of the
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The kilovoltage applied to the x-ra
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Figure 21: Schematic diagram of som
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kind of material radiographed, the
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instance, the kilovoltage may be fi
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The technique need not be limited t
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Chapter 5: Radiographic ScreensWhen
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Contact between the film and the le
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Figure 29: The number of electrons
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lead foil screens ran be retained w
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Figure 33: The sharpness of the rad
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Figure 34: Low density (right) is a
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such as a wall or floor, on the fil
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from this source. Since scatter als
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A filter reduces excessive subject
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Definite rules as to filter thickne
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0.010-inch front screen of value be
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Example: Suppose that with a given
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If the milliamperage remains consta
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- Page 73 and 74: Figure 49: Characteristic curves of
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- Page 77 and 78: Nomogram MethodsIn Figure 54, the s
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- Page 87 and 88: Chapter 8: Radiographic Image Quali
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- Page 91 and 92: Hole Type PenetrametersThe common p
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- Page 127 and 128: DiscussionDensitometric data and pr
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- Page 137 and 138: Methylene-Blue MethodTwo variations
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from the camera or by reaching down
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Figure 106: Schematic diagram of th
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valuable technique, for instance, i
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The position of the spots is determ
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Powder Diffraction File, Internatio
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Processing TechniquesRadiographs on
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Since this formula applies only to
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such that it does not distort the i
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Figure 113: A: Representation of a
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Figure 115: Characteristic curve of
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film fairly well. If high densities
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Density = 1.5 Density = 2.5Film Rel
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In most industrial radiography, the
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e noted here. Although the average
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Chapter 17: Film Graininess; Signal
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The ratio of signal to noise has a
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Chapter 18: The Photographic Latent
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Thus, the change that makes an expo
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Figure 130: Stages in the developme
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electrons by successive Compton int
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Development is essentially a chemic
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Chapter 19: ProtectionOne of the mo
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duct is brought into the x-ray room