Purification of carbon dioxide for reactor purposes, Part III - drying

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dc.contributor.authorDraycott, Aen_AU
dc.contributor.authorKerr, ACen_AU
dc.date.accessioned2007-11-22T04:29:09Zen_AU
dc.date.accessioned2010-04-30T04:39:15Zen_AU
dc.date.available2007-11-22T04:29:09Zen_AU
dc.date.available2010-04-30T04:39:15Zen_AU
dc.date.issued1962-04en_AU
dc.description.abstractComparison of the adsorption characteristics of the desiccants silica gel, alumina, and molecular sieves has shown that molecular sieves have by far the greatest capacity of the desiccants at the low partial pressures considered. Equilibrium data in the form of isotherms were established over the range of variables expected in the coolant circuit of a proposed Australian H.T.G.C. reactor. The mass transfer from the gas phase to molecular sieves is such that no correlation could be attempted for the adsorption zone height; the height proved to be too small.en_AU
dc.identifier.citationPurificationen_AU
dc.identifier.citationDraycott, A., Kerr, A. C. (1962). Purification of carbon dioxide for reactor purposes, Part III - drying. (AAEC/E86). Lucas Heights, NSW: Australian Atomic Energy Commission.en_AU
dc.identifier.govdoc730en_AU
dc.identifier.otherAAEC-E-86en_AU
dc.identifier.urihttp://apo.ansto.gov.au/dspace/handle/10238/720en_AU
dc.language.isoen_auen_AU
dc.publisherAustralian Atomic Energy Commissionen_AU
dc.subjectCarbon dioxideen_AU
dc.subjectReactorsen_AU
dc.subjectAdsorptionen_AU
dc.titlePurification of carbon dioxide for reactor purposes, Part III - dryingen_AU
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