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Colin Judge: Testing structural materials in Idaho’s newest hot cell facility
Idaho National Laboratory’s newest facility—the Sample Preparation Laboratory (SPL)—sits across the road from the Hot Fuel Examination Facility (HFEF), which started operating in 1975. SPL will host the first new hot cells at INL’s Materials and Fuels Complex (MFC) in 50 years, giving INL researchers and partners new flexibility to test the structural properties of irradiated materials fresh from the Advanced Test Reactor (ATR) or from a partner’s facility.
Materials meant to withstand extreme conditions in fission or fusion power plants must be tested under similar conditions and pushed past their breaking points so performance and limitations can be understood and improved. Once irradiated, materials samples can be cut down to size in SPL and packaged for testing in other facilities at INL or other national laboratories, commercial labs, or universities. But they can also be subjected to extreme thermal or corrosive conditions and mechanical testing right in SPL, explains Colin Judge, who, as INL’s division director for nuclear materials performance, oversees SPL and other facilities at the MFC.
SPL won’t go “hot” until January 2026, but Judge spoke with NN staff writer Susan Gallier about its capabilities as his team was moving instruments into the new facility.
Yoshiharu Sakamura, Masaaki Akagi
Nuclear Technology | Volume 179 | Number 2 | August 2012 | Pages 220-233
Technical Paper | Reprocessing | doi.org/10.13182/NT179-220
Articles are hosted by Taylor and Francis Online.
A series of pyrochemical reprocessing tests involving pretreatment, electrolytic reduction, and electrorefining processes were conducted using [approximately]100 g of simulated spent oxide fuel. In the pretreatment process, a simulated spent oxide fuel consisting of dense UO2 pellets containing typical fission product elements (strontium, cerium, neodymium, samarium, zirconium, palladium, and molybdenum) was powderized by voloxidation, which corresponds to fuel decladding. Porous oxide pellets were then fabricated from the obtained oxide powder. In the electrolytic reduction process, [approximately]100 g of the porous oxide pellets was loaded in a cathode basket and electrolytic reduction was performed for 7.6 h in a LiCl-Li2O salt at 650°C. The UO2 was reduced to metallic uranium with a reduction yield of 99.2% and a current efficiency of 74%. All the strontium dissolved into the salt. It was verified that the preparation of porous oxide pellets was highly advantageous in improving the rate of oxide reduction. In the subsequent electrorefining process, the reduction product was loaded in an anode basket and electrorefining was performed for 5.8 h in a LiCl-KCl-UCl3 salt at 500°C. Most of the uranium in the reduction product was anodically dissolved in the salt and the refined uranium metal was collected on a stainless steel cathode. Most of the rare earth elements were dissolved in the salt, whereas zirconium, palladium, and molybdenum remained in the anode residue. The concentration of UCl3 in the salt slightly decreased during electrorefining, since U3+ reacted with the oxides contained in the reduction product to form a uranium oxide precipitate.