1975
DOI: 10.2172/4245488
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1974 operation of the ICPP rare gas recovery facility

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Cited by 3 publications
(4 citation statements)
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“…To avoid possible crystallization in the cryogenic distillation column, the Xe is adsorbed on silica gel at -160 °C and 0.3 MPa. A cryogenic system designed to recover 85 Kr for beneficial use was operated at the Idaho Chemical Processing Plant for a number of years (Brown et al 1983;Hebel and Cottone 1982;Bendixsen and German 1975;Goossens et al 1991;Groenier 1985). The system was designed to treat gases at flow-rates up to 34 -51 m 3 /h (Bendixsen and German 1975).…”
Section: Chalcogel Synthesismentioning
confidence: 99%
“…To avoid possible crystallization in the cryogenic distillation column, the Xe is adsorbed on silica gel at -160 °C and 0.3 MPa. A cryogenic system designed to recover 85 Kr for beneficial use was operated at the Idaho Chemical Processing Plant for a number of years (Brown et al 1983;Hebel and Cottone 1982;Bendixsen and German 1975;Goossens et al 1991;Groenier 1985). The system was designed to treat gases at flow-rates up to 34 -51 m 3 /h (Bendixsen and German 1975).…”
Section: Chalcogel Synthesismentioning
confidence: 99%
“…Irradiation of nuclear fuels results in the production of substantial quantities of various radioactive isotopes. With the establishment of more stringent environmental emission guidelines, several methods •have been proposed for removing these fission products/by-products from contaminated nuclear process off-gases [3,17,29,30,42]. Selective absorption is one of the more versatile processing schemes that has been commercially adapted to the decontamination of different reactor off-gases [5,14,15,39].…”
Section: Disclaimermentioning
confidence: 99%
“…Selective absorption is one of the more versatile processing schemes that has been commercially adapted to the decontamination of different reactor off-gases [5,14,15,39]. Several process solvents, including carbon tetrachloride [23,40], kerosene-base liquids [31], liquid nitrogen [3,4], nitrous oxide [30], liquid carbon dioxide [6,12,13,17,43], dichlorodifluoromethane [24,30,41], and trichlorofluoromethane [25], have been proposed for this and other applications. Considering solvent capacities, separation factors, and thermal and radiation stabilities, as well as overall process safety and economic.features, Steinberg [30] suggested in 1959 utilizing an absorption process employing dichloro~ifluoromethane (refrigerant-12) for stripping the noble gases from contaminated air streams.…”
Section: Disclaimermentioning
confidence: 99%
“…The only feasible approach is to separate and concentrate the Kr for long term storage under controlled conditions. Such a separation has in the past been achieved by cryogenic distillation (Bendixsen et al, 1968(Bendixsen et al, , 1971(Bendixsen et al, , 1973(Bendixsen et al, , 1975Barton, 1974;von Ammon, 1975;Bohnestingl et al. 1976;Chesne et al, 1976;Broothaerts et al, 1976;Kamiya et al, 1975) and also, on a pilot scale, by selective absorption in tluorocarbon solvents (Griftith, 1973, Hogg, 1972Steinberg, 1959;Taylor, 1963;Whatley, 1973;Merriman, 1975).…”
mentioning
confidence: 99%