EP2769384B1 - Décontamination thermique de graphite utilisant des gaz réducteurs - Google Patents
Décontamination thermique de graphite utilisant des gaz réducteurs Download PDFInfo
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- EP2769384B1 EP2769384B1 EP11874351.7A EP11874351A EP2769384B1 EP 2769384 B1 EP2769384 B1 EP 2769384B1 EP 11874351 A EP11874351 A EP 11874351A EP 2769384 B1 EP2769384 B1 EP 2769384B1
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- roaster
- graphite
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- introducing
- carbon
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims description 142
- 229910002804 graphite Inorganic materials 0.000 title claims description 136
- 239000010439 graphite Substances 0.000 title claims description 136
- 239000007789 gas Substances 0.000 title claims description 111
- 238000005202 decontamination Methods 0.000 title description 2
- 230000003588 decontaminative effect Effects 0.000 title description 2
- 238000000034 method Methods 0.000 claims description 53
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical compound [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 claims description 37
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 22
- 239000011261 inert gas Substances 0.000 claims description 22
- 239000001301 oxygen Substances 0.000 claims description 22
- 229910052760 oxygen Inorganic materials 0.000 claims description 22
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 claims description 16
- 230000001590 oxidative effect Effects 0.000 claims description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 13
- 239000001569 carbon dioxide Substances 0.000 claims description 13
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 11
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 239000001272 nitrous oxide Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 229910052786 argon Inorganic materials 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 3
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 150000001298 alcohols Chemical class 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 3
- 229930195733 hydrocarbon Natural products 0.000 claims description 3
- 150000002430 hydrocarbons Chemical class 0.000 claims description 3
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 2
- 229910052734 helium Inorganic materials 0.000 claims description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 2
- 230000008569 process Effects 0.000 description 22
- 238000010926 purge Methods 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 10
- 238000002309 gasification Methods 0.000 description 9
- 230000002285 radioactive effect Effects 0.000 description 9
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 description 8
- VEXZGXHMUGYJMC-OUBTZVSYSA-N chlorane Chemical compound [36ClH] VEXZGXHMUGYJMC-OUBTZVSYSA-N 0.000 description 8
- 238000005007 materials handling Methods 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 6
- 229910052722 tritium Inorganic materials 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000011159 matrix material Substances 0.000 description 5
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000004913 activation Effects 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- OKTJSMMVPCPJKN-IGMARMGPSA-N Carbon-12 Chemical compound [12C] OKTJSMMVPCPJKN-IGMARMGPSA-N 0.000 description 2
- GUTLYIVDDKVIGB-OUBTZVSYSA-N Cobalt-60 Chemical compound [60Co] GUTLYIVDDKVIGB-OUBTZVSYSA-N 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000005549 size reduction Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-OUBTZVSYSA-N Carbon-13 Chemical compound [13C] OKTJSMMVPCPJKN-OUBTZVSYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- XEEYBQQBJWHFJM-BJUDXGSMSA-N Iron-55 Chemical compound [55Fe] XEEYBQQBJWHFJM-BJUDXGSMSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 230000004992 fission Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000002926 intermediate level radioactive waste Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002925 low-level radioactive waste Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002901 radioactive waste Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/28—Treating solids
- G21F9/30—Processing
- G21F9/32—Processing by incineration
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/14—Processing by incineration; by calcination, e.g. desiccation
Definitions
- the present invention relates generally to methods for decontamination of graphite to remove tritium, carbon-14, and chlorine-36 using thermal treatment with purge gases that include reducing gases.
- Graphite which consists predominantly of the element carbon, is used as a moderator in a number of nuclear reactor designs, such as the MAGNOX and AGR gas cooled reactors in the United Kingdom, and the RBMK design in Russia.
- the moderator of the reactor is usually installed as an interlocking structure of graphite bricks.
- the graphite moderator typically weighing about 2,000 tons, is a form of radioactive waste that requires safe disposal.
- Graphite is a relatively stable chemical form of carbon, which is in many ways suitable for direct disposal without processing. However, after neutron irradiation, the graphite will contain stored Wigner energy. The potential for release of this energy needs to be accommodated in any strategy which relies on disposing of the graphite in unprocessed form. Alternatively, processing the graphite before disposal can allow the safe release of any stored Wigner energy.
- the graphite also contains significant quantities of radionuclides from neutron induced reactions, both in the graphite itself and in the minor impurities which it contains. Because of the structure of graphite, which includes loosely packed foliates or layers, the radioisotopes can become trapped within the spaces or pores of the graphite.
- the radioisotope content can conveniently be divided into two categories - short-lived isotopes and long-lived isotopes. Short-lived isotopes (such as cobalt-60) make the graphite difficult to handle immediately after reactor shutdown, but they decay after a few tens of years.
- Carbon-14 is produced in the graphite in one of two ways. One way is the activation of nitrogen gas, with the carbon-14 present in pores of the graphite as carbon dioxide gas. The second way is through the neutron activation of carbon-13, which is a natural, stable isotope of carbon, making up just over 1 percent of the carbon in the graphite. Carbon-14 produced in this way would be part of the graphite matrix. Chlorine-36 is formed in a similar manner by irradiation of chlorine left in the graphite matrix during the graphite sintering process. Processing the graphite offers the opportunity to separate the majority of the graphite mass (carbon) from the long-lived radioisotopes. This processing in turn facilitates disposal of the graphite waste shortly after the end of the reactor life, and may permit recycling.
- Storage has certain negative consequences, such as the following: 1) an implication of long-term financial liability, 2) a visually intrusive storage structure that has no productive purpose, and 3) a requirement imposed on a future generation (which gained no benefit from the original asset) to complete eventual clearance. If the storage alternative is to be replaced by shorter term management, it is essential for the graphite to be processed in a safe and radiologically acceptable manner.
- US 2008/0181835 discloses a system for treatment and recycling of graphite containing radionuclides in a thermal roaster with use of small amounts of oxygen.
- Exemplary embodiments of the present invention provide methods that can subject the graphite to a sufficient temperature range to volatilize the radionuclides without significantly gasifying the bulk graphite.
- One aspect of the invention provides a method that includes the steps of (1) heating a roaster to a temperature between 800° Celsius to 2000° Celsius; (2) introducing graphite contaminated with radionuclides into the roaster; (3) introducing an inert gas into the roaster; (4) introducing a reducing gas into the roaster; and (5) removing volatilized radionuclides from the roaster, wherein a quantity of the reducing gas introduced in the roaster is between 2 and 20% of a whole quantity of gas introduced in the roaster.
- This method may also include the additional steps of:
- the exemplary embodiments of the present invention provide systems and methods for treating radioactive graphite contaminated with tritium, carbon-14, and chlorine-36 and other radionuclides generated during the operation of a nuclear reactor or other nuclear process.
- the systems and methods include a roaster that operates at temperatures in the range of 800° Celsius to 2000° Celsius with inert, optional oxidizing and reducing gases.
- the combination of temperatures and gases allow for the removal of greater than 90 percent of the carbon-14 within the graphite while gasifying less than 5 percent of the bulk graphite.
- FIG 1 depicts a block diagram of a system 100 for treating radioactive graphite in accordance with an exemplary embodiment of the present invention.
- a materials handling component 110 receives graphite to be treated in the system 100.
- the graphite was used as the moderator in a nuclear reactor core.
- Other sources of graphite include, but are not limited to, fuel element sleeves, braces, or other reactor components irradiated by the neutron flux of the reactor.
- This graphite will typically be contaminated with radionuclides such as hydrogen-3 (tritium), carbon-14, chlorine-36, iron-55, and cobalt-60 and may include other typical fission and activation products.
- the material handling component 110 sizes and holds the graphite in preparation for introducing the graphite into a roaster 120.
- the graphite received into the materials handling component 110 would have been removed from the nuclear reactor by any conventional process. These processes may include wet processes, dry processes, or a combination of both.
- the present invention can accommodate either dry or wet graphite in any size or shape resulting from the removal process. Further, the graphite may be soaked in water or other solution prior to being received into the materials handling component 110.
- the graphite may be treated in granular or powdered form.
- a size reducer subcomponent 112 of the materials handling component 110 reduces the size of the received graphite prior to its introduction into the roaster 120. In this exemplary embodiment, the received graphite is reduced to a size less than 20 mm. This small size enhances the volatilization of radionuclides from the graphite.
- the exemplary size reducer subcomponent 112 includes a jaw or rotary crusher. Other size reducing equipment may be used.
- a hopper subcomponent 114 of the materials handling component 110 receives the size reduced graphite and holds the graphite awaiting introduction into the roaster 120.
- the internal atmosphere of the exemplary size reducer subcomponent 112 and hopper subcomponent 114 includes an inert gas blanket, such as argon, nitrogen, carbon dioxide, or other similar inert gas.
- the internal atmosphere of the exemplary size reducer subcomponent 112 and hopper subcomponent 114 is connected to the off-gas system of the roaster 120, as some radionuclides may be released from the graphite during the size reduction process.
- the graphite may be received in a form and size suitable for introduction into the roaster 120 without the need for size reduction.
- a continuous process may omit the hopper subcomponent 114.
- the roaster 120 includes a vessel used to treat the sized graphite.
- the roaster 120 operates in a temperature range of between 800° Celsius to 2000° Celsius.
- the capacity, shape, and size of the roaster 120 can vary by application.
- the roaster 120 is constructed of materials suitable for high temperature operations, such as a refractory-lined steel vessel.
- the operating pressure can vary from a strong vacuum to slightly pressurized. Any type of roaster or apparatus including a fluidized bed, moving bed, batch or static bed roaster can be used.
- One exemplary roaster is a vertically oriented moving bed roaster, where the fresh graphite enters the top of the pile and the treated graphite is removed from the bottom of the pile while the purge gas flow upward (counter current) thru the graphite pile.
- Batch treatment of the graphite would typically involve powdered graphite using a fluidized bed approach.
- a continuous moving bed roaster is preferred.
- the roaster 120 is electrically heated, but other types of heating could be used. Electrical heating is preferred as it reduces the need to introduce oxidizing gases into the vessel, which can gasify the bulk graphite and facilitates temperature control and energy efficiency.
- the roaster 120 receives graphite from a materials inlet 117.
- a variety of mechanical techniques may be used to move the graphite from the materials handling component 110 to the roaster 120 through the materials inlet 117.
- a double valve airlock technique is used to prevent gases from inside the roaster from escaping the roaster and to limit the introduction of gases other than inert gases into the roaster with the graphite.
- the roaster 120 includes gas inlets 130, 140, 150 to receive one or more inert purge gases, one or more reducing gases, and optionally one or more oxidizing gases.
- the gas inlets 130, 140, 150 can be a single inlet connected to three different gas sources, one source providing inert purge gas, a second source providing reducing gas, and a third source providing an oxidizing gas.
- the gas inlet or inlets would be positioned near the bottom of the roaster 120, so that the gases can enter the vessel and travel up through the graphite resident in the roaster 120.
- the gas may be introduced through a flow splitter or distributor to distribute the gas through the volume of graphite, but this component is not required.
- the roaster includes an outlet 122 for volatilized radionuclides, which are carried out of the outlet 122 by the inert purge gas.
- the roaster 120 also includes an outlet 124 for the treated graphite.
- Volatile radionuclides are carried out of the roaster by the purge gas flow and stabilized in treatment subsystem 160, using an appropriate technique for treating the radionuclides.
- the treated graphite is further processed in treatment subsystem 170, where it is packaged for ultimate disposal as "clean" (non-radioactive) waste or is recycled.
- the carbon-14 is more reactive than or more mobile than the bulk carbon-12 in the graphite matrix.
- the presence of small amounts of oxygen provide the oxygen necessary to convert the carbon-14 to carbon monoxide.
- the reducing gases suppress the oxidation of the carbon-12 in the graphite matrix.
- One exemplary benefit of adding reducing gas is that possible carbon-14 compounds in the graphite include cyanide.
- the introduction of hydrogen to the roaster will provide hydrogen atoms to bind with the cyanide to produce hydrogen cyanide, which is volatile, thus some carbon-14 can be removed by the presence of the reducing gas, including hydrogen.
- FIG. 2 depicts a flow diagram of a process 200 for treating radioactive graphite in accordance with an exemplary embodiment of the present invention.
- the graphite is introduced into the roaster 120 from the hopper subcomponent 114 of the materials handling component 110 by a mechanical transfer of the graphite into the roaster.
- the process is performed batch-wise.
- the graphite can be treated in a continuous process, such as where the graphite enters at the top of the roaster 120 and goes out the bottom of the roaster 120 and the reactant gases enter at the bottom of the roaster 120 and go out the top of the roaster 120.
- the hopper subcomponent 114 may be omitted.
- the roaster 120 Prior to introducing the graphite into the roaster 120, the roaster 120 is brought up to treatment temperature. This temperature ranges from 800° Celsius to 2000° Celsius. In this exemplary embodiment, the preferred temperature range is 1200° Celsius to 1500° Celsius, as reducing gases are used in this exemplary process.
- Previous graphite treatment processes for removing carbon-14 from the graphite were limited to temperatures of approximately 1200° Celsius, due to the high gasification of the graphite that resulted from operating a roaster with oxygen containing gases above 1200° Celsius.
- the roaster 120 can operate at temperatures greater than 1200° Celsius. These higher operating temperatures enable the release of essentially all of the tritium, substantially all (greater than 90 percent) of the chlorine-36, and most (greater than 70 percent) of the carbon-14 from the graphite.
- reaction gases are introduced into the roaster 120. These gases contact the heated graphite as they flow through the heated graphite. These reaction gases include at least an inert purge gas and a reducing gas. Purge gases include one or more of nitrogen, argon, or similar non-reactive gas. Inert gases such as carbon dioxide should not be used as these gases would provide an oxygen source that may gasify the bulk carbon. A reducing gas, such as hydrogen, hydrazine, ammonia, carbon monoxide, hydrocarbon vapor, and other reducing gases that can produce free hydrogen, carbon monoxide, or ammonium or organic vapor, is also introduced at step 220.
- a reducing gas such as hydrogen, hydrazine, ammonia, carbon monoxide, hydrocarbon vapor, and other reducing gases that can produce free hydrogen, carbon monoxide, or ammonium or organic vapor, is also introduced at step 220.
- the amount of reducing gas introduced is in the range of two (2) to twenty (20) percent of the total gas introduced and more preferable between two (2) and ten (10) percent.
- This mixture of inert purge gas and reducing gas is introduced into the roaster 120 near the bottom of the roaster 120. The gas moves up through the graphite and carries the volatilized radionuclides out of the roaster 120 at outlet 124. Even with the inclusion of an oxidizing gas, the inclusion of the reducing gas greatly reduces the gasification of the bulk graphite, such that less than five (5) percent of the bulk graphite is gasified.
- reaction gases also include an oxidizer.
- oxygen converts the solid carbon-14 to carbon dioxide or CO gas, which facilitates its diffusion from the graphite matrix.
- the combination of the inert purge gas (preferably nitrogen) with a limited amount of oxygen containing gases, such as steam, carbon dioxide (CO 2 ), nitrous oxide (N 2 O), oxygen (O 2 ), air, alcohols (OH groups), or other oxygenated vapors, and reducing gas, such as hydrogen provides enhanced carbon-14 radionuclide removal compared to all prior techniques while limiting the gasification of the bulk graphite.
- oxygen containing gases such as steam, carbon dioxide (CO 2 ), nitrous oxide (N 2 O), oxygen (O 2 ), air, alcohols (OH groups), or other oxygenated vapors, and reducing gas, such as hydrogen
- the preferred oxidizing gas is steam that would make up approximately one (1) to fifty (50) percent of the total input reaction gases (preferably two (2) to ten (10) percent). If either carbon dioxide or nitrous oxide is used as the oxidizing gas, they would make up approximately one (1) to ten (10) percent of the total input reaction gases.
- the inclusion of the reducing gas greatly reduces the gasification of the bulk graphite in the presence of the oxidizer, such that less than five (5) percent of the bulk graphite is gasified.
- the reducing gas shifts the reaction equilibrium for oxygen with the bulk graphite such that the reaction rate of the oxygen containing gas is substantially inhibited thereby preventing that oxidizer from reacting with the bulk graphite.
- the purge gas is collected in the treatment subsystem 160, where the radionuclides are stabilized using known methods.
- the graphite is removed from the roaster 120 and treated in the treatment subsystem 170. Typically, the treated graphite would be disposed of in a landfill or recycled and would be treated as low-level radioactive waste instead of intermediate-level radioactive wastes.
- the process ends at step 250. The process may be repeated if necessary.
- FIG 3 shows a schematic of an exemplary roaster 300.
- Graphite is introduced through a feeder system (not shown), such as a hopper, at an inlet 310, under a blanket of inert gas.
- Reaction gases are introduced at an inlet 370, such that the reaction gases flow up through the graphite and out the off-gas outlet 320 as the graphite moves down the vessel 330.
- the vessel 330 which may be a ceramic tube, it is heated (depicted as heated graphite 340).
- the vessel 330 is surrounded by a heating source 350, such as electric heating coils.
- the vessel 330 and heating source 350 are contained within an outer vessel 360, such as a refractory-lined metal shell.
- Treated graphite is removed from the vessel 330 through an outlet port 380.
- the present invention provides methods for treating radioactive graphite contaminated with tritium, carbon-14, and chlorine-36 and other radionuclides generated during the operation of a nuclear reactor or other nuclear process.
- the methods include a roaster that operates at temperatures in the range of 800° Celsius to 2000° Celsius with inert gases, reducing gases and optional oxidizing gases.
- the combination of temperatures and gases allow for the removal of most to substantially all the carbon-14 within the graphite while substantially limiting gasifying the bulk graphite.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Environmental & Geological Engineering (AREA)
- Carbon And Carbon Compounds (AREA)
- Furnace Details (AREA)
- Manufacture And Refinement Of Metals (AREA)
Claims (13)
- Un procédé comportant les étapes de :- chauffage d'un four de grillage à une température comprise entre 800° Celsius et 2000° Celsius ;- introduction de graphite contaminé avec de radionucléides dans le four de grillage ;- introduction d'un gaz inerte dans le four de grillage ;- introduction d'un gaz réducteur dans le four de grillage ; et- extraction des radionucléides volatilisés du four de grillage,dans lequel une quantité de gaz réducteur introduite dans le four de grillage est entre 2 et 20% d'une quantité totale de gaz introduite dans le four de grillage.
- Procédé selon la revendication 1 dans lequel moins de cinq (5) pourcents du graphite est gazéifié.
- Procédé selon la revendication 1 dans lequel la température est comprise entre 1200° Celsius et 1500° Celsius,
- Procédé selon la revendication 1 dans lequel les radionucléides comportent du carbone 14 et au moins soixante-dix (70) pourcents du carbone 14 sont extraits du graphite.
- Procédé selon la revendication 1 dans lequel les radionucléides comportent du carbone 14 et au moins quatre-vingt-dix (90) pourcents du carbone 14 sont extraits du graphite.
- Procédé selon la revendication 1 dans lequel le gaz inerte inclut au moins un parmi l'azote, l'hélium et l'argon et le gaz réducteur inclut au moins l'un parmi l'hydrogène, l'hydrazine, l'ammoniac, le monoxyde de carbone et la vapeur d'hydrocarbure.
- Procédé selon la revendication 1 dans lequel le gaz réducteur inclut un ou plus gaz réducteur(s) qui peuvent produire de l'hydrogène libre, du monoxyde de carbone (CO), de l'ammonium ou de la vapeur d'hydrocarbure.
- Procédé selon la revendication 1 comportant en outre l'étape d'ajout de gaz oxydant dans le four de grillage.
- Procédé selon la revendication 8 dans lequel le gaz oxydant inclut au moins un parmi la vapeur, le dioxyde de carbone (CO2), le protoxyde d'azote (N20), l'oxgène (O2), l'air, les alcools (avec groupes OH) ou les autres vapeurs oxygénées.
- Procédé selon la revendication 1 dans lequel les étapes d'introduction du gaz inerte dans le four de grillage incluent l'introduction du gaz inerte et le gaz réducteur au bas du réacteur et dans lequel le gaz inerte et le gaz réducteur s'écoulent à travers le graphite.
- Procédé selon la revendication 1 comportant en outre l'étape de réduction de la taille du graphite avant l'introduction du graphite dans le four de grillage.
- Procédé selon la revendication 1 dans lequel le four de grillage comporte un réacteur à lit mobile, orienté verticalement et dans lequel l'étape d'introduction du graphite contaminé avec des radionucléides dans le four de grillage comporte l'introduction du graphite en haut du four de grillage et dans lequel les étapes d'introduction du gaz inerte dans le four de grillage et d'introduction du gaz réducteur dans le four de grillage comporte l'introduction des gaz en bas du four de grillage.
- Procédé selon la revendication 8 dans lequel une quantité du gaz oxydant ajouté dans le four de grillage est comprise entre 1 et 10% de la quantité totale de gaz introduite dans le four de grillage.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US2011/057301 WO2013058772A1 (fr) | 2011-10-21 | 2011-10-21 | Décontamination thermique de graphite utilisant des gaz réducteurs |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2769384A1 EP2769384A1 (fr) | 2014-08-27 |
EP2769384A4 EP2769384A4 (fr) | 2015-07-22 |
EP2769384B1 true EP2769384B1 (fr) | 2018-10-10 |
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EP11874351.7A Active EP2769384B1 (fr) | 2011-10-21 | 2011-10-21 | Décontamination thermique de graphite utilisant des gaz réducteurs |
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EP (1) | EP2769384B1 (fr) |
JP (1) | JP5844474B2 (fr) |
KR (1) | KR101666138B1 (fr) |
CN (1) | CN104137189B (fr) |
ES (1) | ES2700787T3 (fr) |
LT (1) | LT2769384T (fr) |
WO (1) | WO2013058772A1 (fr) |
ZA (1) | ZA201402825B (fr) |
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FR2997543A1 (fr) * | 2012-10-29 | 2014-05-02 | Electricite De France | Traitement thermique de dechets carbones, perfectionne par le choix des gaz injectes. |
CN106024088B (zh) * | 2016-05-23 | 2017-11-14 | 中国工程物理研究院材料研究所 | 一种放射性污染碳材料的液相氧化消解方法 |
CN106531277B (zh) * | 2016-12-26 | 2018-10-23 | 西南科技大学 | 一种放射性石墨的处理方法 |
CN107051206B (zh) * | 2017-02-16 | 2018-09-21 | 中国科学院上海应用物理研究所 | 一种石墨中氢或其同位素解吸反应釜 |
CN112489847B (zh) * | 2020-12-01 | 2023-05-05 | 中国工程物理研究院核物理与化学研究所 | 一种活化石墨减容处理方法 |
CN113257450B (zh) * | 2021-03-30 | 2023-11-10 | 北京交通大学 | 一种退役放射性核石墨的处理方法 |
CN113429224B (zh) * | 2021-05-14 | 2022-10-04 | 中国工程物理研究院材料研究所 | 一种碳材料的表面刻蚀方法 |
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JP2633000B2 (ja) * | 1989-01-28 | 1997-07-23 | 動力炉・核燃料開発事業団 | 高放射性廃棄物の処理方法 |
US5183541A (en) * | 1990-04-09 | 1993-02-02 | Westinghouse Electric Corp. | Decontamination of radioactive metals |
UA57884C2 (uk) * | 1999-10-14 | 2003-07-15 | Дейвід БРЕДБЕРІ | Спосіб обробки радіоактивного графіту |
GB2445420A (en) * | 2007-01-05 | 2008-07-09 | Tetronics Ltd | Hazardous Waste Treatment Process |
US20080181835A1 (en) * | 2006-12-01 | 2008-07-31 | Mason J Bradley | Steam reforming process system for graphite destruction and capture of radionuclides |
FR2943167B1 (fr) * | 2009-03-11 | 2011-03-25 | Electricite De France | Traitement de dechets radioactifs carbones. |
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- 2011-10-21 WO PCT/US2011/057301 patent/WO2013058772A1/fr active Application Filing
- 2011-10-21 JP JP2014537046A patent/JP5844474B2/ja active Active
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WO2013058772A1 (fr) | 2013-04-25 |
JP2014532855A (ja) | 2014-12-08 |
KR20140101735A (ko) | 2014-08-20 |
EP2769384A1 (fr) | 2014-08-27 |
EP2769384A4 (fr) | 2015-07-22 |
CN104137189A (zh) | 2014-11-05 |
ZA201402825B (en) | 2016-01-27 |
JP5844474B2 (ja) | 2016-01-20 |
CN104137189B (zh) | 2017-07-25 |
RU2014120424A (ru) | 2015-12-10 |
ES2700787T3 (es) | 2019-02-19 |
KR101666138B1 (ko) | 2016-10-13 |
LT2769384T (lt) | 2018-12-27 |
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