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U.S. Department of Energy
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Control of the reduction/oxidation potential of Hanford Waste Vitrification Plant feeds

Conference ·
OSTI ID:6817093

A schematic diagram shows the various processing steps to be performed during feed preparation in the Hanford Waste Vitrification Plant (HWVP). The pretreated NCAW is transferred to the slurry receipt adjustment tank (SRAT) in the HWVP for concentration. Water removed during boildown is collected in the slurry mix evaporator condensate tank (SMECT). After waste treatment the water is returned to the storage tanks for eventual disposal. The pretreated Neutralized Current Acid Waste (NCAW) is concentrated in the SRAT to approximately 125 g waste oxides/ liter. Formic acid is then added at a controlled rate to improve rheological properties and achieve a required reduction/oxidation state. Reflux boiling is initiated and continued for several hours. The concentrated slurry is cooled and pumped to the slurry mix evaporator (SME). In the SME, glass frit is added, and the slurry is further concentrated to achieve a nominal composition of 500 g total oxides/liter. This waste/frit slurry is transferred to a melter feed tank (MFT) and continuously metered to a joule-heated ceramic melter where it is converted into a borosilicate glass. 2 figs.

Research Organization:
Westinghouse Hanford Co., Richland, WA (USA)
DOE Contract Number:
AC06-87RL10930
OSTI ID:
6817093
Report Number(s):
WHC-SA-0269; CONF-880903-33; ON: DE89000514
Country of Publication:
United States
Language:
English