3 SRS Composite Inventory Salt SupernateVolumeCuriesSaltcake18.1 Mgal183 MCi(46%)Salt Supernate(48%)34.4 Mgal196 MCi(91%)(52%)16.3 MgalSaltcake12 MCi(45%)(3%)3.3 Mgal184 MCi(9%)(48%)Sludge37.7 Million380 MillionGallons (Mgal)Curies (MCi)SludgeInventory values as of
4 Interim Salt Processing TK 49 TK 50 ARP (HTF: 96-H) MCU (HTF: 278-H) ARP (DWPF: 512-S)ReceiptTankMSTStrike TankTK 49FeedTankPrecipTankFiltrate HoldTankCrossflowFilterReceiptTankMSTStrike TankSolventHoldTankWTL (DWPF: 221-S)InterimSalt ProcessingPRFTStrip EffluentDecanterContactorsSRATSEFTARP – Actinide Removal Process – removal of actinides (AN #89 through A# Thorium, Protactinium, Uranium, Neptunium, Plutonium, Americium, Curium etc) and StrontiumMCU – Modular Caustic Side Solvent Extraction Unit – Removal of Cs 137ARP / MCU - Radioactive operations – spring 2008 – one year of operation to date – will run until SWPF comes online .About 365,000 gallons have been fed to ARP / MCU to date (about 4000 gallons per batch).Processing flow rate is 4 gpm.Complex system - note that ARP / MCU is in H Tank FarmVITRIFICATIONStrip EffluentHold TankDSSDecanterSSMixing TankSSReceipt TankTK 50DSSHold TankVaultSaltstone
5 Saltstone Processing Processed 3.7M gallons of salt solution total Processed 1.4M gallons since start of current campaign in March 2007Processing Rate – 120K gallons / wkVault 2 Under ConstructionBackground – just in case it comes up –March 5, DDA processing initiated (Deliquification, dissolution, and adjustment)Late March 2007 – legal appeal filed, Saltstone processing suspended.October 2007 – Legal appeal resolved. Processing resumes.Vault M gallons grout / 192 CiVault M gallons grout / 134,000 Ci total inventoryOriginal design – Ci/galCurrent design – 0.1 to 0.2 Ci/galOriginal Design capacity K gallons / weekRecent failure of grout pump hose - expect to return to Tank 50 processing by approximately mid-April.Vault 2 construction completion in July 2010Vault 2 – two concrete tanks with a total useful volume of 667,000 ft3. Equivalent to about 3 cells of the old vault design. About 35 weeks operating volume.
6 Salt Waste Processing Facility 98M Gallons Salt Solution to be processedFull Construction Authorization (CD-3)Transition to Radioactive Operation - May 2013CD-3 received late FY08Schedule contingency – 124 weeks (31 months) to January 2016
7 Salt Disposition Integration Project Prepare initial macrobatch feed for SWPFReady to feed SWPF by a rate of:3.75M gallons / yr – first year6M gallons / yr – normal rateReady to process 220K gal/wk from SWPF to SaltstoneReady to process Strip Effluent and MST Sludge Solids from SWPF to DWPF
8 HLW Processing Overview 2696 Canisters Produced (thru March 31)2.82 M Gallons transferred from HTF97 Canisters – FY 09 (thru March 31)Processing Sludge Batch 5 thru May 2010Melter 2 – Operational Since March 2003Melter 3 – Ready as SpareMelter Vessel and Frame contract awardedK3 Refractory – Manufacturing In progressComponents – Under constructionAssembly completion date – November 2013Over 10.5 Million Pounds of HLW Glass18.4 Million Cicanisters poured by Melter 1canisters poured by Melter 2Planning basis – High Fe sludge – 250 canisters per year / High Al sludge – 186 canisters per year.Sludge Batch 5 – low temperature Aluminum dissolution conducted for this batchSludge Batch 6 processing in progress – will also undergo LTADSystem Plan Rev 15 – Sludge processing complete in FY30
9 Issues and Challenges Tank Closure Canister Fissile Loading – Processing limitations897 g/m3Sludge Batch 5 limited to 33 wt % waste loadingConstruction and Startup of SWPFTotal Canister ProductionAvailability of Federal RepositoryRecently completed acid cleaning in two type I waste tanks in F Area. Started mechanical cleaning in two type IV waste tanks in F Area (sand mantis to remove zeolite resin mounds from CRC units) Two type IV tanks previously closed in F AreaSWPF – Current operational date of May Parsons is responsible for the design, construction, and first year of operation of the facility.High Al Sludge – higher viscosity melt – lower heat transfer rate – lower melt rate – lower canister production rate - investigating new frit formulations, improvements to existing melter operationTotal Canister Production – System Plan Rev canisters (with mitigation – new melter technology, higher waste loading, with Al removal)Maintaining all future canisters below 897 g/m additional canistersNo mitigation (no new melter technology or higher waste loading) additional canisters - need to confirm numbers2244 canisters stored in GWSB#1 (99.6% of capacity)449 canisters stored in GWSB#2 (19.2% of capacity)GWSB #3 - needed by FY Is in the planning baselinePlanning Basis was to start shipments in FY 17FY17 – 130 canisters/ yearFY canisters / yearFY19 – 500 canisters / year
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