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Thermal Treatment of Magnox Sludge Intermediate Level Nuclear Waste through Vitrification
Sean T. Barlow BSc (Hons) AMInstP Martin C. Stennett1, Russell J. Hand1, Sean P. Morgan2 & Neil C. Hyatt1 1. Department of Materials Science & Engineering, The University of Sheffield, Sheffield S1 3JD, UK 2. Sellafield Ltd., Hinton House, Risley, Warrington WA3 6GR, UK Scientific Basis for Nuclear Waste Management Symposium 2017, October 29 – November 3 | Sydney, Australia Good morning everyone, as you’ve just heard name is Sean Barlow and I’m a PhD student at the University of Sheffield’s Immobilisation Science Laboratory and my presentation this morning is on the work I have done on formulating glass compositions for the vitrification of UK Magnox Sludge.
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Worlds first civil nuclear power station
1956 – Calderhall Worlds first civil nuclear power station 1950’s Queen visited Sellafield to open the Calderhall reactors – worlds first. Americans had proven it first, Russians first to connect to a grid (not civil use). Pic at bottom shows Queen inspecting the top of the reactor core, machine in middle used to de-fuel and re-fuel the reactor. Overall pic of the site under operation. 4 reactors in separate buildings and each with a dedicated cooling tower (away from the coast). Design went through several variations over the decades resulting finally in the last to be built at Wylfa in North Wales.
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Wylfa 2015 Research impetus
Various designs of Magnox plant, 11 station and 26 reactors in UK + exports Magnox fleet of reactors used unenriched uranium metal clad in a Magnesium non-oxidising (Magnox) alloy (99% Mg, 1% Al) Magnox fuel elements Magnox design of power stations went through various different iterations during the 60 years of operation. Pictured on the top is Wylfa which was last Magnox reactor to shut down at the very end of No cooling towers needed as it’s by the sea, both reactors in one building. What is the problem… Almost 60 years of atomic power in the UK has created large quantities of nuclear waste a significant quantity of which is from the Magnox fleet of reactors. These reactors used natural uranium metal fuel clad in a magnesium alloyed called Magnox which is 99% Mg and 1% Al.
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Background First Generation Magnox Storage Pond (FGMSP)
Spent fuel from all 26 Magnox reactors in the UK was sent to be reprocessed at Sellafield but was first stored underwater in huge ponds such as the FGMSP pictured The material was stored underwater to reduce the radiological hazard however due to industrial action in the 1970s and 1980s, a build-up of nuclear fuel for reprocessing occurred which meant that the material was stored underwater for longer than anticipated. Sites are aging and it is a priority to empty the silos asap. Seagull in pond potentially spreading contamination
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Background Magnox Swarf Storage Silos (MSSS)
Spent fuel from all 26 Magnox reactors in the UK was sent to be reprocessed at Sellafield but was first stored underwater in huge ponds such as the FGMSP pictured on the top. After reprocessing, the sheared Magnox cladding, called swarf, was also stored underwater in the MSSS. The material was stored underwater to reduce the radiological hazard however due to industrial action in the 1970s and 1980s, a build-up of nuclear fuel for reprocessing occurred which meant that the material was stored underwater for longer than anticipated.
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Over 3148 m3 of consolidated sludge to treat at Sellafield
Magnox corrosion Magnox sludge retrieval at the Sellafield site Over 3148 m3 of consolidated sludge to treat at Sellafield Current plan Baseline treatment plan is encapsulation in cement matrix 3m3 box used for cement encapsulation Cross-section of cement ILW So when you add metal to water corrosion occurs, and in the case of Magnox material the corrosion product is magnesium hydroxide which is a sludge like material lining the bottom of the ponds. Metallic uranium has also partially corroded meaning both U metal and U oxides are incorporated into this sludge making it one of the most contaminated sites in Western Europe. The baseline plan for dealing with this waste is encapsulation in a cement matrix, but this has 2 key drawbacks. Firstly, there is difficulty in predicting the long-term durability of the cemented waste and secondly there is a significant increase in volume of waste to deal with. So an alternative is needed.
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Current plan Cementation has two key drawbacks:
Difficulty predicting long-term durability Significant increase in waste volume Alternative wasteform needed to improve safety case & save on cost of geological disposal
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Vitrification Proven technology for immobilisation of high level waste
2-D Schematic network of an alumino-borosilcate glass Natural analogue, Obsidian Proven technology for immobilisation of high level waste Radiation resistant and potential for high waste loadings Can incorporate wide spectrum of elements Long-lived natural analogues (obsidian) In this project we propose vitrification since it is already a proven technology for the immobilisation of HLW. Glass wasteforms can also incorporate most of the elements in the periodic table, are resistant to radiation damage and have the potential for high waste loadings. However the most important feature is its longevity. The natural analogue, obsidian, dates back to the Cretateous period millions of years ago, so we can be therefore be confident that our nuclear waste glass will remain intact over hundreds of thousands of years. Vitrified HLW
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Previous work O Between 33-37 wt% waste loadings
RLB: (1.40 ± 8.3) x 10-2 g/m2/d RLU: (3.45 ± 0.01) x 10-5 g/m2/d Previous work MAS glass with corroded waste MAS glass with metallic waste MBS glass with corroded waste MBS glass with metallic waste MBS-M O Mg Si U Vitrification can save up to £82 million ($100 million) Between wt% waste loadings
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Surrogate compatibility
Use of other elements to simulate uranium Looked into neodymium and mischmetal (lanthanide alloy) Replaced U in MBS and MAS samples on a molar basis Same melting conditions 1250 °C for 3 hours (MBS) 1500 °C for 5 hours (MAS) Nd glass under incandescent light Nd glass under fluorescent light
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U, Nd, Mm Uptake Sample Mol% oxide batched Mol% oxide in glass
Uptake into glass (oxide) % MBS-M (U) 14.5 6.9 47.6 MBS-M (Nd) 5.2 4.9 94.2 MBS-M (Mm) 7.8 4.2 53.8 Sample Mol% oxide batched Mol% oxide in glass Uptake into glass (oxide) % MBS-C (U) 1 0.7 70.0 MBS-C (Nd) 0.9 0.4 44.4 MBS-C (Mm) 0.5 80.0
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X-Ray diffraction U samples: Oxide crystals
Nd samples: Mix of oxide and borate crystals Mm samples: Borate crystals
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Scanning electron microscope
Nd samples: ~15 µm B Nd Si Mm samples: ~15 µm B Ce La U samples: Small crystallites ~5 µm Fractal pattern
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Long-term durability All samples show similar pH behaviour
MAS samples higher pH than MBS
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Long-term durability Nd shows similar trend to U most likely pH dependent. Mm samples… More oxidation states possible – more aqueous phases ∴ more dissolution
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Conclusions & Further Work
A single glass formulation (MBS) can be used to treat both extremes of the waste expected in Sellafield’s Magnox sludge – previous study. Mischmetal comparable to Uranium for uptake into glass structure Neodymium and Mischmetal for borate phases – larger crystal size than uranium Neodymium comparable for dissolution studies, Mm larger amount of OS possible Determine the oxidation state of Nd and Mm samples Raman spectroscopy – structure of the glass This research serves to provide more effective, detailed knowledge into vitrified glass as a potential wasteform for the disposal of Sellafield's Magnox sludges
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Thank you for listening!
Special thanks to: Prof Neil C. Hyatt Prof Russell J. Hand Dr Martin C. Stennett Dr Claire L. Corkhill Dr Sean P. Morgan Mr Adam J. Fisher Mr Daniel J. Bailey & the ISL team Thank you for listening! The authors would like to thank the EPSRC (Grant EP/G037140/1) for funding this research which was performed in part at the MIDAS Facility, University of Sheffield, established with support from the Department of Energy and Climate Change.
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