- Page 1 and 2: Nuclear Science Pyrochemical Separa
- Page 3 and 4: OECD PROCEEDINGS Proceedings of the
- Page 5: FOREWORD In the future, nuclear fue
- Page 8 and 9: J. Uhlir Pyrochemical Reprocessing
- Page 10 and 11: Annex 1. LIST OF PARTICIPANTS......
- Page 12 and 13: In the poster session, eight poster
- Page 14: OPENING SESSION 11
- Page 18 and 19: OPENING ADDRESS Philippe Savelli De
- Page 20: SESSION I National and Internationa
- Page 23 and 24: A sixth project might be funded by
- Page 25 and 26: Selective extraction of minor actin
- Page 27 and 28: Work programme The work programme i
- Page 29 and 30: Introduction Commercial nuclear pow
- Page 31 and 32: The ATW system is predicated on the
- Page 33 and 34: In the electrorefiner, the transura
- Page 35 and 36: these materials will be sent direct
- Page 37: alternative were to be used instead
- Page 41 and 42: Introduction Global awareness of pr
- Page 43 and 44: Concerning on oxide fuel reprocessi
- Page 45 and 46: Military plutonium conversion to MO
- Page 47 and 48: The study on radiation conditions d
- Page 49 and 50: Figure 3. Flowsheet of pyroelectroc
- Page 51 and 52: Introduction Processing of nuclear
- Page 53 and 54: drossing or slagging, and volatilis
- Page 55 and 56: BNFL electrorefiner programme Progr
- Page 57 and 58: If oxide fuels are to be treated by
- Page 59 and 60: with international organisations in
- Page 61 and 62: Figure 1. Uranium active rig hall B
- Page 63 and 64: For the immediate future, the proje
- Page 66 and 67: ROLE OF PYROCHEMISTRY IN ADVANCED N
- Page 68 and 69: On the contrary, the metal refining
- Page 70 and 71: REFERENCES [1] R.J.M. Konings, R. C
- Page 72 and 73: Figure 1. Transition of U-fuelled L
- Page 74: Table 1. Gibbs’ energies for fluo
- Page 77 and 78: The present interest in the develop
- Page 79 and 80: 9. The supporting fuel matrices hav
- Page 81 and 82: REFERENCES [1] R.C. Robertson, ORNL
- Page 83 and 84: Introduction Since 1985, the CRIEPI
- Page 85 and 86: Injection casting of metallic fuels
- Page 87 and 88: REFERENCES [1] T. Inoue and H. Tana
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EVALUATION OF PYROCHEMICAL REPROCES
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cathode is confirmed at laboratory
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Reduction of environment impact In
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Improvement of recovery Pyrochemica
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Figure 1. Pyrochemical flowsheet fo
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SESSION III Part A: Basic Data (The
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Introduction Systematic investigati
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The experimental results of heat ca
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A preliminary assessment of the ava
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Figure 1. Heating thermogram of EuC
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Figure 7. Partial pdfs, gαβ(r) Fi
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ELECTROCHEMICAL PROPERTIES OF PLUTO
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Results and discussion Electrochemi
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The largest activity coefficient of
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in which K* 1 and K* 2 are calculat
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[16] A.S. Kertes, Actinides Rev., 1
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Figure 4. Cyclic voltammogram and i
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APPLICATION OF ELECTROCHEMICAL TECH
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Ln 3 + + 3e − ↔ Ln (3) M+ + e
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99.9%). A three-electrode device wa
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The mean value of the coverage quan
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[11] W. J. Wruck, R. M. Machado and
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Figure 5. Chronopotentiogram for th
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THERMODYNAMIC STABILITIES OF LANTHA
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Electromotive force determination f
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0 in Table 1. The observed close-to
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REFERENCES [1] H. Moriyama, H. Yama
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Figure 1. Dependence of ∆G ex [M
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SESSION III Part B: Results and Exp
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Introduction In processing of spent
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which could result if the highly en
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The uranium content is about 4% by
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Figure 2. Schematic of the Mark IV
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NITRIDE/PYROPROCESS FOR MA TRANSMUT
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In the case of UN, we later identif
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REFERENCES [1] T. Mukaiyama, et al.
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Figure 3. Stability diagram of U-N-
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PYROMETALLURGICAL REDUCTION OF UNIR
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The pyrochemical furnace has three
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In the case of experiments with a s
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The experiments consume about 1-2 g
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Table 3. Comparison of analytical r
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Figure 5. Variation of Pu concentra
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Introduction The interest in pyrome
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Development of electrorefiner The e
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[7] Y. Sakamura, T. Hijikata, T. In
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Figure 4. Chlorination step Cl2 gas
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Photo 3. The electrorefiner install
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Introduction Pyrochemical reprocess
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In some of the experiments, UO2 dis
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Figure 1. Laboratory scale facility
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SESSION III Part C: Process Simulat
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Introduction Within the solution of
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Basic requirements these components
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The longest measured time of deform
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KINETICS OF PYROCHEMICAL PROCESSING
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Mass transfer coefficient It is imp
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elatively large radius, will diffus
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[11] S. Forcheri and V. Wagner, Z.
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A RATIONAL APPROACH TO PYROCHEMICAL
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This is a fundamental point to work
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Thus the literature data generally
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NaCl+KCl mixture Figure 6 demonstra
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[13] L. Joubert, G. Picard, B. Silv
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Figure 3. GPTD 2-D diagrams summari
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Figure 7. Chemical actions of chlor
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OPEN DISCUSSION AND RECOMMENDATIONS
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POSTER SESSION 231
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Introduction EXAFS and NMR are prom
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At the 99 Tc NMR spectrum of Tc met
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Scheme 1. Possible Tc species in py
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Figure 3. Temperature dependence of
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MOLTEN SALT BURNER FUEL BEHAVIOUR A
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Nuclear design and fuel cycles flex
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could be achieved in the absence of
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Preliminary thermodynamic considera
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Summary Though the molten salt nucl
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Table 1. Thermodynamic properties o
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RECOVERY OF NOBLE METALS (RU, RH, P
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Tellurium oxide extraction: Experim
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Processing by hydrogen during the d
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Figure 1. Free enthalpy of various
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Figure 5. Data of kinetics of the
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Introduction Japan Nuclear Cycle De
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To discuss the influence of reactio
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Figure 1. Temperature dependency of
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Figure 7. Relation between oxide ra
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PARTITIONING OF AMERICIUM METAL FRO
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The published relevant thermodynami
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REFERENCES [1] J. Malvyn, Mckibben,
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Table 1. Reported americium valency
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Figure 2. Standard free energy of f
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AMERICIUM EXTRACTION VIA IN SITU CH
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Introduction The purification of pl
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At 800°C the dissociation of pure
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Table 3. Distribution of americium
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Figure 3. XR Diffractogram of CaCl
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Introduction The lanthanide element
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The coefficients are described by t
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Thus using the values of potential
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Conclusion The electrochemical redu
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Figure 3. The dependencies of peak
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GENERALISED PERTURBATION THEORY AND
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∑ dV dN i j ∫ =−Ni dV i k k
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or the influence of other parameter
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Appendix A THE PROBLEMS OF THE DEPE
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5. Calculate via gradient method co
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FRANCE Dr. Michel ALLIBERT INP Gren
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Mr. David LAMBERTIN CE Valrhô (DCC
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INDIA Mr. Krishnamruthy NAGARAJAN H
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SPAIN Dr. Concepcion CARAVACA CIEMA
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Dr. Lothar KOCH Head of Nuclear Che
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Annex 3 STATE-OF-THE-ART REPORT ON
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NEA Publications of General Interes
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