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Outline of EU Processing Salvage Operations – Recovering uranium from salvage and by-products Uranium Purification – Separating uranium from impurities.

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Presentation on theme: "Outline of EU Processing Salvage Operations – Recovering uranium from salvage and by-products Uranium Purification – Separating uranium from impurities."— Presentation transcript:

1 Outline of EU Processing Salvage Operations – Recovering uranium from salvage and by-products Uranium Purification – Separating uranium from impurities – Producing pure uranium compounds Uranium Metal Production – Converting uranium compounds to pure metal Machining

2 Why Discuss EU Processing? Understanding the process is key to performing an adequate NCS analysis! – A lack of understanding might lead to excessive conservatism - complicated controls – Might lead to a failure to evaluate credible conditions – incomplete controls

3 Sources Enriched Uranium Processing, Patton, Googin, and Griffith, Pergamon Press Inc. (1963). Nuclear Chemical Engineering, Benedict, Pigford, and Levi, McGraw-Hill Inc. (1981)

4 Salvage Operations - Overview Concentration of Combustibles by Ignition – Graphite, absorbent paper, PPE (gloves, booties, etc), filters, etc. – Muffle furnacing – Destructive distillation Leaching – Recovering uranium from ash and other insoluble materials – Dissolving/acidifying uranium compounds

5 Salvage Operations - Furnaces Muffle Furnace – Single retort (closed vessel with outlet), typically electric – Combustible batch in a pan – Furnace is supplied air or O 2 – Produces a stable uranium-laden ash – Exhaust gas contains entrained uranium and is filtered

6 Muffle Furnace

7 Salvage Operations - Furnaces Destructive Distillation – Retort and distillate tank – Combustible batch in a pan – First cycle is distillation – Second cycle is oxidation – Produces a stable uranium laden ash and organic distillate – Distillate and exhaust gas should not contain much entrained uranium

8 Destructive Distillation

9 Leaching Acid washing insoluble materials laden with uranium Continuous or batch Geometry/volume control preferable: – Volume (beakers, flasks, etc.) – Geometry (cylindrical tanks, slab tanks, trays) Uranium solution is the product Leached solids discarded (after confirmation)

10 Uranium Purification Summary Separating uranium from impurities – Solvent extraction – Evaporation Production of pure uranium compounds – Molten uranyl nitrate – Denitration – Fluid bed reactors

11 Solvent Extraction Selectively removing uranium from aqueous solution using organic solvents Stripping uranium from organic into clean aqueous solutions EU recovery may involve two separate solvent extraction processes – primary and secondary Utilizes nitric acid chemistry

12 Salting Uranyl nitrate: UO 2 (NO 3 ) 2 Highly soluble in water UO 2 (+2) + 2NO 3 (-1) ↔ UO 2 (NO 3 ) 2 Balance between ions and undissociated Nitrate salts push the equilibrium toward the undissociated molecule Undissociated molecule soluble in many organics solvents (ethers, ketones, and alcohols) – Not paraffins (such as kerosene)

13 Salting Agents Common salting agents include nitric acid and ammonium, sodium, calcium, and aluminum nitrates Aqueous feed is loaded with salting agent to favor extraction in organic solvent

14 Distribution Coefficient Concentration of component (uranium) in organic phase to that in aqueous phase From Benedict, Pigford, and Levi

15 Organic Solvents Dibutyl Carbitol (DBC) – with high nitrate and low acid concentrations, DBC is efficient in removal of uranium – Product has lower uranium concentration than feed Tributyl Phosphate (TBP) – Nitric acid is an efficient salting agent with TBP – High density of TBP requires use of hydrocarbon diluent – Very little nitric acid extracted – Higher uranium concentrations in aqueous effluent (raffinate)

16 Solvent Extraction Flow Sheets From Benedict, Pigford, and Levi

17 Solvent Extraction Flow Sheets From Benedict, Pigford, and Levi

18 Types of Extraction Equipment From Benedict, Pigford, and Levi

19 Primary and Secondary Extraction Primary: uses DBC – Advantages: scavenges uranium from feed, produces low uranium raffinate – Disadvantage: requires substantial salting, product has low uranium concentration Secondary: uses TBP diluted in hydrocarbon – Advantages: requires little salting, produces clean product – Disadvantages: high uranium concentration in raffinate

20 Evaporation Process Condensate Steam Condensate

21 Evaporation Natural circulation Evaporation rate regulated by steam pressure Entrained liquid removed (cyclone and demisters) returned to evaporator Acid and water vapors condensed Steam and process condensates discarded Product withdrawal and feed rate regulated to maintain target concentration

22 Production of Pure Uranium Compounds Denitration Precipitation Reduction

23 Denitration Thermal decomposition of UO 2 (NO 3 ) 2 to UO 3 Evolves water, NOx gasses, and uranium particulate Stirring action mills the powder particles Walls are heated Product overflows an adjustable dam Gasses and particulate are treated in a packed column (dissolver/scrubber)

24 Stirred-bed Denitrator From Patton, Googin, and Griffith

25 Precipitation

26 pH carefully monitored Precipitate nonstoichiometric Consistency of gelatin Must be dewatered – filtered or centrifuged Filtrate or centrate discarded; will contain residual uranium as light, suspended solids Product collected in container (furnace crucible or pan)

27 Supplemental Notes on Uranium Compounds Precipitates are converted to dry solids – UO 3 – produced at lower temperatures – U 3 O 8 – produced at higher temperatures – UO 2 – higher temperatures, requires H and absence of O 2, product unstable in air – UF 4 – produced from oxide reaction with HF Higher surface area particles are more reactive Calciners, furnaces, fluid beds, stirred beds

28 Uranium Metal Production Reduces UF 4 to uranium metal by reaction with highly pure magnesium or calcium Reactant metal is uniformly mixed with UF 4 and charged to the reactor – Typically in a crucible and with a sand liner – Lid secured tightly (energetic reaction) High temperature required during and after reaction to promote separation of U from slag

29 Typical Bomb Reduction Assemblies From Patton, Googin, and Griffith

30 Uranium Metal Production Contents of the reactor mechanically separated Metal regulus is cleaned (pickled) Slag discarded (could be used as salting agent for solvent extraction) Liner fragments discarded Sand discarded or reused

31 Machining Cutting uranium metal generates heat and requires coolant to prevent fires involving turnings (chips, fines) Turnings are valuable and are collected for recovery Typically significant amounts are machined to remove surface defects from casting

32 Machine Lathe

33 Machining Metal

34

35 Machine Turnings


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