Acknowledgments Financial support for this research was provided by the European Commission (project ACSEPT – Contract No. FP7-CP-2007-211 267). References [1] Bourg, S., Caravaca, C., Ekberg, C., Hill, C., Rhodes, C. ACSEPT, Toward the Future Demonstration of Advanced Fuel Treatments. Proceeding of International Conference GLOBAL <strong>2009</strong> (The Nuclear Fuel Cycle: Sustainable Options & Industrial Perspectives), Paris, 6–11 September <strong>2009</strong>, paper 9185, pp. 937–943. , www.acsept.org [2] Sasaki, Y., Sugo, Y., Suzuki, S., Tachimori, S. (2001) The novel ex-tractants diglycolamides, for the extraction of lanthnides and actinides in hno3-n-dodecane system. Solvent Extraction and Ion Exchange, 19(1), pp. 91–103. [3] Tachimori, S., Sasaki, Y., Suzuki, S. (2002) Modification of TODGA-n-dodecane Solvent with a Monoamide for high loading of Lanthanides(III) and Actinides(III). Solvent Extraction and Ion Exchange, 20(6), pp. 687–699. [4] Modolo, G., Asp, H., Schreinemachers, C., Vijgen, H. (2007) Development of a TODGA based Process for partitioning of actinides from a PUREX raffinate Part I: Batch extraction optimization studies and stability tests. Solvent Extraction and Ion Exchange, 25(6), pp. 703–721. [5] Modolo, G., Asp, H., Vijgen, H., Malmbeck, R., Magnusson, D., Sorel, C. (2008) Demonstration of a TODGA-Based Continuous Counter-Current Extraction Process for the Partitioning of Actinides from a Simulated PUREX Raffinate, Part II: Centrifugal Contactor Runs. Solvent Extraction and Ion Exchange, 26(1), pp. 62–76. [6] Magnusson, D., Christiansen, B., Glatz, J.P., Malmbeck, R., Modolo, G., Serrano-Purroy, D., Sorel, C. (<strong>2009</strong>) Demonstration of a TODGA based Extraction Process for the Partitioning of Minor Actinides from a PUREX Raffinate Part III: Centrifugal Contactor Run using Genuine Fuel Solution. Solvent Extraction and Ion Exchange, 27(1), pp. 26–35. [7] Serrano-Purroy, D., Baron, P., Christiansen, B., Malmbeck, R., Sorel, C., Glatz, J-P. (2005) Recovery of minor actinides from HLLW using the DIAMEX process. Radiochimica Acta, 93(3), pp. 351–355. [8] Serrano-Purroy, D., Christiansen, B., Glatz, J-P., Malmbeck, R., Modolo, G. (2005) Towards a DIAMEX process using high active concentrate. Radiochimica Acta 2005, 93 (3), 357–361. [9] Hérès, X., Sorel, C., Miguirditchian, M., Camès, B., Hill, C., Bisel, I., Espinoux, D., Eysseric, C., Baron, P., Lorrain, B. (<strong>2009</strong>) Results of recent counter-current tests on An(III)/Ln(III) separation using TODGA extractant. Proceeding of International Conference GLOBAL <strong>2009</strong> (The Nuclear Fuel Cycle: Sustainable Options & Industrial Perspectives), Paris, 6–11 September <strong>2009</strong>, paper 9384, pp. 1127–1132. [10] Geist, A., Modolo, G. (<strong>2009</strong>) TODGA Process Development: an Improved Solvent Formulation. Proceeding of International Conference GLOBAL <strong>2009</strong> (The Nuclear Fuel Cycle: Sustainable Options & Industrial Perspectives), Paris, 6–11 September <strong>2009</strong>, paper 9193, pp. 1022–1026. 73
5.7. Synthesis and thermal treatment of uranium-based microspheres through internal gelation H. Daniels, S. Neumeier, G. Modolo Corresponding author: g.modolo@fz-juelich.de Abstract An alternative to the direct final disposal of long-lived radionuclides is their separation (partitioning) from the original waste in connection with a subsequent appropriate treatment. The general aim is to lower the risk potential coming along with the radioactivity (radiotoxicity). A promising concept after the partitioning step is the embedding of Am, Cm & Np, the “Minor Actinides” (MA), in uranium-based nuclear fuel (co-conversion). Through this the MAs can be eliminated by nuclear reactions with fast neutrons (transmutation) in upcoming reactor concepts. One way to obtain such fuel is the internal-gelation process: Amorphous gel-spheres are created and thermally treated at comparably low temperatures to become crystalline. The main advantages are the high automation potential as well as the co-conversion being carried out predominantly in aqueous solutions without dust-creation. The formulation of stable precursor solutions for the gelation is one crucial step towards a reliably working process. Therefore MA-surrogates were utilised for basic research on reaction mechanisms and speciation in the corresponding aqueous phases. Subsequently, the UO 2 -based ceramics obtained through thermal treatment of the gels were characterised to optimise the calcination and sintering process. Introduction Advanced nuclear fuel management with the help of new reactor generations needs appropriate fuel matrices. A UO 2 based fuel with addition of minor actinides can serve as a fuel and transmutation matrix in parallel. Fabrication of such fuels has high demands due to radiotoxicity and contamination issues. A procedure minimising the connected risks is highly beneficial. Internal gelation is a well known method to produce microspheres suitable as sphere-pac fuel or as precursors for fuel pellet fabrication. One variant of internal gelation was developed in <strong>Forschungszentrum</strong> <strong>Jülich</strong> by Förthmann et al. [1] In contrast to KEMA- and similar processes [2], the gelating agents were added in solid form. The advantage of this variant is the resulting higher effective uranium concentration in the precursor solution due to a less overall volume of water needed for solvation of the chemicals. Therefore, the preparation of acid deficient uranyl nitrate (ADUN), which leads to a higher uranyl solubility, is nonessential [1]. The work in <strong>2010</strong> focused on the investigation of chemical interactions between the involved species in solution and the thermal treatment of obtained uranium / neodymium microspheres through internal gelation. For the experiments, neodymium was utilized as a surrogate for a trivalent actinide such as americium. Additionally, creation ADUN through 74
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Mitglied Mitglied der der Helmholtz
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Forschungszentrum Jülich GmbH Inst
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TABLE OF CONTENTS 1 Preface .......
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6.2.2 Doctoral Thesis .............
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state of NRW. The collaborative pro
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2 Institute’s Profile Due to the
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2.2. Organization chart Reactor Saf
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3 Key Research Topics 3.1. Long Ter
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actinide co-conversion into polyact
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Fig. 7: Non-destructive analytical
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Fig. 9: Thermal treatment of an AVR
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3.8. Product Quality Control of Rad
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The relative uncertainty for the ac
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In the drum, 4 ‘hot spots’ for
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activity of Cs-137 is much more und
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gamma-ray detector approximated by
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shown in Fig. 96. In both cases the
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econstruction than the old calculat
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Neutron capture cross sections and
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Outlook The evaluated data will be
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from carbon-based HTR fuel elements
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Fig. 102: 3D volume reconstructions
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dislocate the 14 C atom from its pr
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It can be seen that nearly all trit
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Acknowledgement The authors like to
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development by investigations of ga
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Fig. 109: The left picture shows th
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[2] A European Roadmap for Developi
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from airborne SWIR Full Spectrum Im
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Fig. 113: Visualization of the vege
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number of training samples up to 19
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Acknowledgements The work presented
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three approaches has severe drawbac
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neighbours from the list of merge c
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it gives a difference in segmentati
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[6] I. Niemeyer, F. Bachmann, A. Jo
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Monitoring 3 cooperated intensively
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facilities and other treaty related
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parameters of the SAR system, such
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The MGD products used in the study
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Fig. 134 contains the result for th
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[2] H. Maître (ed.), Processing of
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Preparatory Committee to allocate t
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unconditional security assurances f
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safeguards was also requested. Deci
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[16] United Nations Security Counci
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5.24. Development and Application o
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Hardware layer The hardware layer i
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So in most applications the scale u
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The ENDF-B/V and ENDF-B/VI librarie
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5.26. Product control of waste prod
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Polysiloxane which has been investi
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acceptance requirements [3]. In the
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Fig. 145: List of description and d
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6.1. Courses taught at universities
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Umwelt / Energy & Environment 2010;
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6.5. Institute Seminar The IEK-6 or
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6.5.3 Invited talks 2009 30.04.2009
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21.09.2010 Dr. N. Evans: The Chemis
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8 Selected R&D projects 8.1. EU pro
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K. Aymanns: Nominated as deputy re
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Bukaemskiy A.A., Barrier D., Modolo
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Rezniczek, A.; Richter, B.; Jussofi
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Daniels, H.: Co-conversion of actin
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Sypula, M.; Wilden, A.; Schreinemac
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(Partitioning) - Stabilitätsunters
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Modolo, G.; Bosbach, D.; Geist, A.;
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12 How to reach us Postal Address F
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By train: Take the train from Aache
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Schriften des Forschungszentrums J
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Schriften des Forschungszentrums J
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