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The Savannah River Site is the U.S. Department of Energy's preferred site for
return and treatment of all aluminum-base, spent, research and test reactor
fuel assemblies. There are over 20,000 spent fuel assemblies now stored in
different countries around the world, and by 2035 many will be returned to SRS
for treatment and interim storage, in preparation for disposal in a geologic
repository.
The early fuel assemblies for research and test reactors were made using
aluminum clad plates that were fabricated from highly enriched (93%)
uranium-aluminum alloy. Later, powder metallurgical fabrication methods were
developed to produce plate fuels with higher uranium contents using either
uranium aluminide, uranium oxide or uranium silicide powders mixed with
aluminum. Silicide fuel elements generally are fabricated with low enriched
uranium containing less than 20% 235U. Following irradiation, the
spent fuel assemblies are discharged from the reactor, and most assemblies have
been stored in under-water pools, some since the early 1950's.
A number of disposition options including direct/co-disposal and melt-dilute
treatment were evaluated recently. The melt-dilute technique was identified as
the preferred method for treatment of aluminum-base spent fuel. The technique
consists of melting the spent fuel assembly and adding depleted uranium to the
melt for isotopic dilution to <20% 235U. Aluminum is added, if
necessary, to produce a predetermined alloy composition. Additionally, neutron
poisons may be added to the melt where they form solid solution phases or
compounds with uranium and/or aluminum. Lowering the enrichment reduces both
criticality and proliferation concerns for storage. Consolidation by melting
also reduces the number of storage canisters.
Laboratory and small-scale process demonstration using irradiated fuel is underway. Tests of the off gas absorption system have been initiated using both surrogate and irradiated RERTR mini fuel plates. An experimental L-Area facility (LEF) is planned to validate induction furnace operations, remote handling, and the off gas system for trapping volatile elements under plant operating conditions. Results from laboratory tests and the small-scale process studies are discussed.
The U.S. Department of Energy (DOE) is consolidating at the Savannah River Site (SRS) both foreign and domestic spent research and test reactor fuel assemblies that originated in the United States. These transferred assemblies are presently stored on site in water basins until a treatment and interim storage facility is available. The DOE through SRS has evaluated direct/co-disposal and melt-dilute technologies and has identified Melt-Dilute Treatment Technology (MD) as the preferred alternative for ultimate disposal of spent nuclear fuel in the Draft Environmental Impact Statement(1). The record of decision on spent fuel management is expected late this calendar year.
During the next 30-40 years, SRS will receive and store approximately 28 metric tons of heavy metal (MTHM) from spent nuclear fuel. This material may be treated and dry stored at SRS in a "road ready" canister until a geologic repository is available. About three quarters of the fuel by volume is in the form of high-enriched uranium (HEU) and could present criticality control issues during storage that are not inherent to low enriched (LEU) fuel disposition. The melt-dilute option will reduce the alloy isotopic enrichment to < 20% by diluting the material with depleted uranium thereby reducing concerns over criticality and proliferation. This method also decreases SNF volume by about 70% while producing a robust waste form for long term storage.
Early research and test reactor fuels were manufactured using cast aluminum-uranium alloy containing highly enriched uranium (93% 235U). Fuel plates of MTR type were clad with aluminum alloys and bonded to the meat section by hot and cold rolling methods. Later, powder metallurgical techniques were developed for fuel meat fabrication using either blended UAlx or U3O8 and aluminum powders. Finally, to increase uranium fuel density, aluminum silicide fuels were developed in the 70-80's, and are now used to make low enriched uranium fuel elements for research and test reactors. After irradiation many fuel assemblies have been stored at reactor sites in under-water fuel basins (some as long as 30 years after discharge from the reactor).
The melt-dilute (MD) process for treatment of spent fuel has been under development at SRS for several years. The flow diagram for this process is shown in Figure 1. Initially, the spent fuel assembly is loaded into a crucible/liner arrangement placed in a commercial induction furnace. Depleted uranium is added to lower the isotopic content, and aluminum to adjust the final composition. The melt is stirred by induction stirring to accomplish the isotopic dilution. In the case of oxide based fuels, the charge is held at temperature to allow for reduction of this oxide by aluminum or other additions. After this, the melt is sampled to insure compositional consistency. Finally, the alloy is furnace cooled in the crucible to produce an ingot for storage. During the entire process the gases released from the melt are treated through an off-gas system designed to trap radionuclides and volatile fission products.
The melt-dilute process development has included bench-scale studies using surrogate and irradiated spent fuel. In addition, small-scale studies using MTR equivalent surrogate spent fuel materials (using depleted uranium alloys) was also conducted to evaluate the off-gas system concepts to trap volatile fission products released from spent fuel assemblies during the melt and dilute process. Currently, a small-scale facility capable of demonstrating and validating the melt-dilute process using single irradiated MTR elements is being designed and assembled in the L-Reactor Area at SRS. This facility is referred to as the L-Area experimental facility (LEF). The DOE has considerable experience in the melting of aluminum-uranium fuel materials and limited experience in the melting of irradiated spent fuel. The melt-dilute process operations differ from aluminum-uranium casting primarily in the radiation field and the volatility of some fission products associated with spent fuels. These factors necessitate the development of remote operations (i.e., stirring and sampling) and of the off-gas system. The off-gas system consists of zeolite adsorption beds for the adsorption of volatile fission products and HEPA filters to ensure the entrapment of condensed particles. The melt-dilute system consisting of an induction furnace and off gas adsorption beds are contained inside a steel enclosure that is located inside a shielded concrete facility. All operations are conducted remotely from a control room using an overhead crane and a hardened camera system.
Figure 1. Melt-Dilute Process Flow Diagram
Before fuel loading, the stainless steel top of the furnace enclosure is
removed. The spent fuel assembly, removed from the transportation cask, is
placed in a consumable aluminum basket. The basket including the spent fuel is
put inside the crucible/liner. Depleted uranium for isotopic dilution (<20%)
and aluminum for compositional control (13.2 wt% Al-U alloy) are added to the
crucible/liner before startup. The amount added is based on initial
calculations. The off-gas system including the absorption bed is then located
on top of the crucible and the furnace enclosure top replaced.
The melt-dilute process cycle is approximately 6 hours including the approximate 1 hour it takes to completely melt and dilute one MTR assembly, induction stirring and melt-sampling. The temperature of the eutectic composition is the lowest liquidus temperature (646 °C) in the binary uranium-aluminum system but the process is expected to operate at 850 ± 50 °C. This will provide sufficient super heat to adequately dissolve the uranium diluent and minimize volatilization of some fission products. The cooling time needed to reach the solidus temperature is approximately 5 hours. Once solidified the ingot and carbon steel liner is removed from the furnace and stored in a storage canister.
Fundamental experimental investigations of the solidification microstructure
resulting from different processing treatments have been carried out in order
to provide information for the development of the melt and dilute processing
technology for cast U-Al, and Al-UAlx,
Al-U3Si2, and Al-U3O8 powder
metallurgy research test reactor fuel assemblies. These investigations have
been centered on binary uranium-aluminum alloys with compositions at or near
the eutectic (13.2 wt % U) but have included ternary additions to simulate
processing of silicide and oxide fuel assemblies. Development of ternary
isothermal sections for the U-Al-Si using the standard Gibbs triangulation
technique and fundamental thermodynamic calculations assessing the possible
reaction paths in the U-Al-O system have been performed. Additionally,
fundamental dissolution kinetic experiments have been conducted using depleted
U3O8 and U3Si/U3Si2
samples and molten aluminum. The microstructures of dip samples as well as
sections from the cast form were characterized using light optical microscopy,
X-ray diffraction, scanning electron microscopy, and energy dispersive
spectroscopy. Additionally, chemical analysis was performed using ICPES.
Additional melting experiments were performed at ANL-East using irradiated SNF coupons. The test specimens used in this test consisted of 1.25" x 0.5" x 0.06" strips of UAlx fuel with Al-2Mg cladding. The original loading of the entire fuel assembly from which these strips were sectioned was 1.7 gU/cc with a beginning of life enrichment of 44.9%. The average burnup of this assembly was 74%. For this test, the irradiated SNF coupons were placed in a graphite crucible and heated in the test assembly at 850°C for 1 hour.
U-Al Fuels and Alloys: Many MTR and other research reactor fuel elements were originally fabricated using highly enriched uranium (93 wt%
Figure 2 Binary Equilibrium Uranium-Aluminum Phase Diagram(2)
Figure 3 Photomicrograph of typical irradiated UAlX fuel plate (a)
and
a backscattered electron micrograph of a simulated fuel plate after the
melt and dilute process (b).
U-Al-Si Fuels and Alloys: Fuels based on the U-Si system have been developed by the Reduced Enrichment Research and Test Reactor program operated by Argonne National Laboratory, which has worked for the past 15 years to develop low enriched (<20%) uranium alloy fuel for use in research and test reactors. Examination of the U-Si binary equilibrium phase diagram shows two compounds possessing high atomic uranium fraction: U3Si and U3Si2. Research and test reactor fuels using these two compounds have been manufactured as fuel core composites consisting of powder metallurgy blends of Al powder and the individual uranium-silicide compounds. They are expected to be approximately 20% of the fuel inventory to be treated by the melt-dilute process
The aluminum-uranium-silicon ternary phase diagram was developed using the Gibbs triangulation method and experimental data. Isothermal sections were studied to determine the liquid phase region at the expected fuel composition. At 800°C a significantly large liquid phase region exists at the aluminum rich end of the ternary phase diagram as shown in Figure 4. Thus, treatment of these fuels should be similar to the uranium-aluminum alloy fuels and similar process operating parameters are expected. In Figure 5, a typical photomicrograph of the fuel core from a silicide fuel assembly (a) shows interaction between the uranium-silicide intermetallic and the Al matrix. The new phase formed is the U(Al,Si)3 which is the one of the equilibrium phases for this mixture3. Also included in this figure is a photomicrograph showing the resultant microstructure of a melt and dilute processed silicide fuel assembly (b).
Figure 4 Aluminum-Rich Corner of the Aluminum-Uranium-Silicon isothermal section of the ternary phase diagram at 800 ºC.
Figure 5 Photomicrograph of typical irradiated U3Si2 fuel plate (a) and a micrograph of a simulated fuel plate after the melt and dilute process (b).
Oxide Fuels and Alloys: Like the silicide fuels the uranium oxide fuel particles react with the aluminum matrix while in service as is evident from Figure 6a. However, the extent of the reaction in the oxide is much greater than in the silicide fuels. At 850°C, thermodynamic calculations indicate that the reaction between uranium oxide and aluminum is favorable. Unfortunately, the reaction kinetics are relatively slow at this temperature. For example, Figure 6b is a micrograph of an oxide fuel element simulation after the melt at 850°C for 3 hrs. Large particles of partially reduced UO2 are still present. It is expected that the slow reaction kinetics are a result of the formation of a stable aluminum oxide layer at the particle-liquid interface. However, the addition of small amounts of calcium to the melt greatly increases the reaction rate making the processing time similar to U-Al alloy fuel. In Figure 6c, the resulting microstructure of a similar test with small additions of calcium (i.e., ~5%) shows complete reduction of the uranium oxide at 850°C in less than 1 hour.
Figure 6 Photomicrograph of typical irradiated Al + U3O8
fuel plate (a) a micrograph of a simulated fuel plate after 3hrs at 850ºC
(b)
and a simulated fuel plate after the melt and dilute process with small
additions of calcium(c).
A critical technology element in the development of the melt-dilute process is
the development of an off-gas system. The volatilization of radioactive
fission products during the melting stage of the process constitutes the
off-gas. The challenge for the melt-dilute treatment process is to capture
these volatile fission products and radionuclides. With this in mind an
analytical and experimental program has been undertaken to assess the
volatility and capture of species under the melt-dilute operating
conditions.
Thermodynamic calculations were performed for uranium-aluminum fuels to
determine elements that may be released when melting. Types and quantities of
fission products and radionuclides were calculated for a 250 MWd MTR assembly
after 5 years cooling using the Origin-S computer code. Based on an ideal
solution model, elemental vapor pressures, and an air flow rate through the
system of 1 scfm, it was determined that the fission product of most concern
was cesium. Other elements remained in the melt either because they had a low
vapor pressure or because they formed compounds within the melt having low
vapor pressures. Gaseous fission products, such as I, Kr, and tritium will be
completely released during melting however, preliminary calculations show that
for both on-site and off-site individuals the effective dose equivalents do not
exceed regulatory limits..
Actual fission product release experiments have been conducted within the DOE complex with respect to research and test reactor safety and core melt-down scenarios (3-7). These experiments clearly showed that noble gases and cesium vapors are released from Al-based fuels. Two major outcomes from these sets of experiments are as follows:
Throughout these experiments the release of cesium has been shown to be a
nonlinear function of burnup, atmosphere, temperature, and fuel
composition.(7)
Additionally, because of the published variability of cesium release data and testing conditions two sets of fission product release tests have been performed at SRTC and ANL-East. The SRTC tests employed non-radioactive fission product surrogates in full-scale melt-dilute melts and the ANL-East test used bench-scale irradiated SNF coupons. These ANL tests using RERTR mini-fuel plate sections were done in the Alpha-Gamma Hot Cells at ANL East. These tests were carried out using conditions that closely mock up the melt-dilute process. Plate samples (~5 gram size) were placed into a graphite crucible and heated at 850 °C for 1 hour with a 1 scfm air flow rate through the crucible and zeolite bed. The purpose of the tests was to determine fission product release, to verify thermodynamic calculations, and to determine the effectiveness of a zeolite sorption bed in capturing volatized fission products. A water scrubber was used to capture any volatile fission products that may break-through the zeolite bed.
After heating the crucible, piping and zeolite bed were gamma scanned, and the scrubber solution was analyzed for fission product activity of elements that might escape the sorption bed. A typical gamma spectrum from the crucible and absorber bed is shown in Figure 7.
Figure 7 ANL Results from RERTR Fuel Melt Experiment.
When the cell background is subtracted from the gross activity, as shown by the
lower curve in the figure, it was found that 78% 137Cs remained in
the solidified ingot. Of the fraction released, 16% was located at the bottom
few centimeters of the zeolite bed, and 6% plated out on the stainless steel
tubing leading from the crucible to the sorption bed. No other volatile
elements were detected on the bed, and no activity was found in the wet
scrubber solution; therefore, complete sorption of volatile cesium occurred on
the bed. At 850°C, 22% of the cesium was released from the melt in this
study.
The analytical and experimental tests conducted at both SRTC and ANL, have identified cesium as the melt constituent of most concern with respect to volatilization. Experimental tests using both cesium surrogates and radioactive cesium have confirmed previous data by Hoe(8)and Wolkoff(9) that zeolite 4A is an effective cesium trap, and as a result a preliminary off-gas system concept has been developed employing dry zeolite 4A adsorber beds as the primary cesium trapping medium. Validation of this off-gas concept will occur during full-scale irradiated testing in the proposed L-Area Experimental Facility.
Design of the off-gas system for the LEF pilot-scale facility is based on
experimental results obtained from laboratory tests and from the ANL study of
irradiated samples. The system layout is shown in Figure 8. The induction
furnace as well as the primary and secondary adsorber beds is located inside a
steel enclosure (confinement space). There is a negative pressure differential
between the room, enclosure and furnace crucible, so any air leakage is into
the crucible and is exhausted through the off gas HEPA system. Also, inside
the enclosure is the secondary absorption bed which serves as a backup in the
event breakthrough occurs during melting. From the secondary bed, the off gas
is directed through a dual bank of HEPA filters to remove particulate
particles. After passing through the system, the off-gas is discharged to the
stack. Nobel gases released are expected to be within current regulatory
guidelines, but if not, gases such as iodine and krypton can be captured using
charcoal and low temperature silver mordenite beds,(10)
respectively.
Initially, six assemblies will be melted for evaluation; the need for
additional tests will be determined after analysis of the data from the first
six tests. The initial six assemblies will range from an aluminum-depleted
uranium surrogate assembly for equipment and process checkout to assemblies
with increasing burnup to 50%. Since, each assembly will have a higher burnup
the level of Cs-137 will increase with each test. The purpose of these tests
is to evaluate current process parameters and off-gas system design. Data
obtained will include absorber bed performance and efficiency, dilution
composition, and crucible/liner performance. The design of the off-gas system
for the full-scale irradiated fuel assembly facility will be based on data
obtained from the bench-scale and full-scale surrogates tests as well as the
bench-scale irradiated SNF coupon test.
Figure 8 Melt-Dilute Off-gas system Flow Diagram for the LEF Facility.
Preliminary investigations using both surrogate and irradiated SNF coupons have been conducted at SRTC and ANL to validate the melt-dilute treatment technology process and off-gas development. Through bench-scale and full-scale surrogate testing, the melt-dilute treatment technology has been shown to effectively treat all of the Al-based research and test reactor fuel types. Furthermore, with regard to the off-gas system development studies, experiments conducted at SRTC and ANL with surrogate and irradiated materials have shown that zeolite 4A is an effective medium for trapping gaseous cesium vapors. Finally, validation of these experiments will be demonstrated in a full-scale irradiated melt-dilute facility to be constructed in L-Area at SRS.
The authors gratefully acknowledge the support, melt testing, and gamma analysis of RERTR fuel plate samples by Adam Cohen and his staff at Argonne National Laboratory-East.