future nuclear fuel cycles prospects and challenges
play

FUTURE NUCLEAR FUEL CYCLES : PROSPECTS AND CHALLENGES D. WARIN, B. - PowerPoint PPT Presentation

The Tenth OECD Nuclear Energy Agency Information Exchange Meeting on Actinide and Fission Product Partitioning and Transmutation FUTURE NUCLEAR FUEL CYCLES : PROSPECTS AND CHALLENGES D. WARIN, B. BOULLIS CEA, Nuclear Energy Division 1 Main


  1. The Tenth OECD Nuclear Energy Agency Information Exchange Meeting on Actinide and Fission Product Partitioning and Transmutation FUTURE NUCLEAR FUEL CYCLES : PROSPECTS AND CHALLENGES D. WARIN, B. BOULLIS CEA, Nuclear Energy Division 1 – Main achievement in the frame of 1991 Act 2 – P and T in the 2006 Act 3 – Fuel cycle possible options 4 – On going R and D programs IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 1/22

  2. The 1991 French Act: frame of the Program � 3 Research thematics: December 30, 1991 ● partitioning and transmutation of LLRNs ● deep repository ● confinement and interim storage � Deadline : final report in 2006 IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 2/22

  3. Minor Actinide Partitioning strategy Spent Fuel PUREX U, Pu Np Two step strategy CO-EXTRACTION Fission DIAMEX Products of MAs and Ln SEPARATION SANEX Ln Am, Cm of Mas from Ln IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 3/22

  4. DIAMEX demonstrative hot run, Nov. 2005 PUREX raffinate 15 kg genuine fuel NaOH HEDTA HEDTA Solvent Treatment HNO 3 Am ~ 150 mg/L (ECRAN) HNO 3 Cm ~ 15 mg/L H 2 C 2 O 4 Ln ~ 2.5 g/L HEDTA 4 m high V ~ 1 L/h HNO 3 Pulsed columns H 2 C 2 O 4 HEDTA Back-extraction An-Ln - Scrubbing (MS) extraction extraction extraction extraction FP An+ Ln An+ Ln (CP) (CP) HNO 3 (CP) (CP) (CP) (CP) 0.65 M DIAMEX DMDOHEMA/TPH Production Am, Cm, Ln Am ~ 0.015 % Am, Cm, Ln FP Cm < 0.002 % Raffinate > 99.9% IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 4/22

  5. SANEX demonstrative hot run, December 2005 HNO 3 NaOH HEDTA extraction-scrubbing DIAMEX Solvent DMDOHEMA 0.5 M Production + HDEHP 0.3 M Am, Cm, Ln TPH HNO 3 ~ 45 mL/h Raffinate Am, Cm < 0.01% Ln An stripping Ln stripping scrubbing Ln HEDTA HNO 3 Am, Cm > 99.9% An Citric ac. Am < 0.06 % F.D.Ln ~ 80 Cm < 0.03 % IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 5/22

  6. The 2006 French Act � PRINCIPLES : ● Recycle (reprocess) June 28, 2006 to decrease waste amount and toxicity ● Retrievable Geological Repository , the reference option for ultimate waste management � A « ROADMAP » : ● 2012 : industrial potentialities of the diverse P&T options, and prototype by 2020 ● 2015 : repository defined, and operation by 2025 IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 6/22

  7. The 2006 French Act (Article 3) PARTITIONING and TRANSMUTATION OF LLRNs « The research in this field will be connected to research concerning the new generation of nuclear reactors , as well as accelerator driven systems devoted to waste transmutation, in order to have, by 2012, an evaluation of the industrial potentialities of these concepts, and in order to start operating a prototype before December 31st, 2020 … » IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 7/22

  8. Minor Actinide Partitioning : what processes ? � Solvent extraction, first ! ● Already developed at commercial plant scale (Industrial potentiality) ● high separation yields ! ● low amount of secondary waste ! � The main alternative: Pyro_processes IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 8/22

  9. Future fuel cycle options : the 2012 milestone � Define the several options of interest, which could be successively deployed (all-actinide, Americium only, heterogeneous, homogeneous,…) � Assess benefits /costs ratio for the several recycling options, considering diverse criteria and “densification” of the final storage � Design / Optimize separation processes, transmutation fuels and their fabrication processes � and gather technical elements for industrial operation evaluation IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 9/22

  10. Future fuel cycle options, Reactor and Treatment U U U R T FP R T FP R T FP&MA MA Pu U Pu U Pu AM U MA heterogeneous U and Pu recycled, MA homogeneous recycling recycling PUREX U « double strata » U FP R T FP&MA R T MA U Pu U Pu ADS U and Pu recycled, T COEX IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 10/22

  11. Fuel cycle, the « COEX TM » concept URANIUM TREATMENT REACTOR FPs & MAs Pu and U U - U and Pu recycling, extraction-fabrication - without anywhere, anytime « pure » plutonium - suitable for Gen3 and MOX-LWRs - a first step before more advanced options ? IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 11/22

  12. Fuel cycle, the MA heterogeneous recycling option URANIUM FPs REACTOR TREATMENT MAs Pu,U,(Np) U - U, Pu, Np by COEX TM (or PUREX) - Am (and Cm) separation : DIAMEX, SANEX,… - Am (and Cm) recycled on dedicated « targets-blankets » IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 12/22

  13. Fuel cycle, the MA heterogeneous recycling option DIAMEX-SANEX with extractant separation DMDOHEMA HTP EXTRACTION / SCRUB. (DIAMEX process) DMDOHEMA Solvent treatment F.P. PUREX HNO 3 HNO 3 (except Ln+ Y) raffinate HEDTA. oxalic acid DMDOHEMA HTP Acidic extractant HTP Extractant separation Ln STRIPPING An STRIPPING pH > 5 DTPA or HEDTA Am + Cm HNO 3 Ln + Y Glycolic acid pH 3 (hot test scheduled in 2009) IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 13/22

  14. Fuel cycle, the MA homogeneous recycling option URANIUM FPs REACTOR TREATMENT Pu, U, MAs U - U, Pu, Np by COEX TM + Am (and Cm) by DIAMEX-SANEX - or all-actinide grouped management (GANEX), the most advanced option, but drawbacks for fuel cycle operation IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 14/22

  15. Fuel cycle, the GANEX concept RECYCLE Spent fuel DISSOLUTION DISSOLUTION UPuNpAmCm Conversion U 1 st step U Extraction Pu+MA 2 nd step Ln Stripping An Stripping F.P. Ln Ln WASTE IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 15/22

  16. Fuel cycle, the GANEX hot runs in Atalante 1st step : U selective extraction Solvent Mono Amide clean-up (performed successfully Extraction Scrubbing U stripping in June 2008) Np, Pu, Am, Cm + Feed HNO 3 U Diluted FPs HNO 3 U > 99.9% 2nd step : Pu-Np-Am-Cm co-recovery (diamide-based process) (scheduled in November 2008) IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 16/22

  17. Fuel cycle, from MA solutions to fuels Actinide oxalic co-conversion (precipitation, filtration, calcination) ATALANTE – L15 Atalante/L15 U 70 % - Pu 30 % Continuous operation U, Pu,Np U, Pu, Np, Am U 78 % - Pu 20 % - Np 1% - Am 1 % COPIX (UPu)O 2 irradiation test in Phénix, 2008-2009 IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 17/22

  18. CEA Pyro reference route: reductive extraction Fluoride Salt An AnF 3 AlF 3 Salt before extraction Al An Al Metal Solvent Actinide distribution coefficients >100 An/Ln separation factors > 1000 • Attractive potentialities : Salt after extraction • Compactness • No radiolytical effects • Suitable for advanced fuels, hot fuels • … • but still heavy work, still questions: • Operating pyro-processes at industrial scale ? • Technological waste amount ? IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 18/22

  19. Separation process : CEA on going R and D � COEX TM : « Demo runs » ( separation, conversion, COPIX) � DIAMEX, SANEX : ● Single cycle flowsheets ● « Am only » recovery concepts � GANEX : ● 1 st and 2 nd cycles ● New flowsheets considered… � Atalante new hot runs : from 2008 to 2012 � PYRO: Stripping in molten salts (after extraction) IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 19/22

  20. Separation process : consolidation towards industrialization Long term effects (solvent treatment) O O H 3 C CH 3 N Modeling N C 8 H 17 C 8 H 17 C 2 H 4 (flowsheet, sensitivity, operation) O C 6 H 13 Extractant Core of the process demonstrated at small scale synthesis DMDOHEMA + HDEHP An(III) + Ln(III) Ln(III) An stripping Extr-scrub. Ln stripping DTPA Raffinat pH 3-4 Ln PF An PUREX FP solution adapted Interface to vitrification Co-conversion Equipments (Concent. Calcination) (Implementation, In situ extrapolation) analysis (cations, pH...) IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 20/22

  21. New workshops at La Hague Areva plant ? MINOR ACTINIDE PILOT SFR MOX FUEL FABRICATION (remote fabrication) (the core of SFR proto (experimental pins, ASTRID, tons) MONJU demo, kg) IEMPT-10, Mito, Japan, October 8, 2008 Radiochemistry and Processes Department 21/22

Download Presentation
Download Policy: The content available on the website is offered to you 'AS IS' for your personal information and use only. It cannot be commercialized, licensed, or distributed on other websites without prior consent from the author. To download a presentation, simply click this link. If you encounter any difficulties during the download process, it's possible that the publisher has removed the file from their server.

Recommend


More recommend