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ORAU TEAM Dose Reconstruction Project for NIOSH

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Document No. <strong>ORAU</strong>T-TKBS-0041 Revision No. 01 Effective Date: 06/02/2009 Page 16 of 89<br />

Figure 2-2. Apollo site floor plan.<br />

2.1.3.2 Various Uranium Process Activities<br />

A general description of processes <strong>for</strong> various enrichments of uranium at Apollo is outlined in AEC<br />

Health and Safety Laboratory (HASL) Survey Reports 82, 92, 103, 106, and 114 (Occupational<br />

Exposure to Radioactive Dusts reports) which cover the period from December 1959 to January 1961<br />

and the Procedures <strong>for</strong> Recovery of Uranium Scrap from about 1963. (AEC 1960a,b,c, 1961a,b;<br />

NUMEC ca. 1963). The following paragraphs provide a description of the process.<br />

Production of UO3 from UF6 began with UF6 being converted to UO3 in the Chemical Conversion<br />

Room. A 5-in. diameter UF6 cylinder was removed from a shipping/storage container known as a<br />

“birdcage” and placed in a heating mantle connected to the system, and brought to operating<br />

temperature and pressure. The UF6 gas was fed at a controlled rate into a water-circulating column<br />

where the UF6 was hydrolyzed to an aqueous solution of UO2F2 and HF. This solution was then piped<br />

to a second column where it reacted with NH4OH to <strong>for</strong>m a slurry of ammonium diuranate (ADU),<br />

((NH4)2U2O7). The slurry was then pumped through a hooded pressure filter. The filter cake was<br />

scraped off, placed in shallow metal containers called fry pans, and transferred to drying hoods where<br />

the ADU was decomposed at a controlled temperature to UO3. The UO3 was transferred from the<br />

pans to small polyethylene containers in an unvented glovebox and subsequently transferred to<br />

Ceramics Fabrication <strong>for</strong> further processing (AEC 1960a, p. 3). The HASL-92 (AEC 1960b, p. 2)<br />

survey from August 1960 noted that the filter cake was dried by means of a rotary kiln rather than the<br />

previous fry pan method. HASL-114 (AEC 1961b, p. 2) survey from June 1961 noted that a calciner<br />

was added <strong>for</strong> reduction of ADU to U3O8. The dried cake was then discharged directly from the kiln<br />

into a container, eliminating the manual transfer.<br />

NOTE: While not specifically stated in the HASL reports, the removal of the filter cake from the<br />

pressure filter might have been a manual operation. No in<strong>for</strong>mation could be found to indicate that<br />

the filter scraping was automated or that it was per<strong>for</strong>med in a glovebox or under a filter hood.

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