EP0281680A1 - Method of cleaning a spent fuel assembly - Google Patents
Method of cleaning a spent fuel assembly Download PDFInfo
- Publication number
- EP0281680A1 EP0281680A1 EP87118413A EP87118413A EP0281680A1 EP 0281680 A1 EP0281680 A1 EP 0281680A1 EP 87118413 A EP87118413 A EP 87118413A EP 87118413 A EP87118413 A EP 87118413A EP 0281680 A1 EP0281680 A1 EP 0281680A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fuel assembly
- chamber
- alkali metal
- fuel
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 31
- 238000004140 cleaning Methods 0.000 title abstract description 15
- 239000002915 spent fuel radioactive waste Substances 0.000 title description 9
- 239000000446 fuel Substances 0.000 claims abstract description 65
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 32
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 32
- 230000002285 radioactive effect Effects 0.000 claims abstract description 17
- 239000011261 inert gas Substances 0.000 claims abstract description 11
- 238000001816 cooling Methods 0.000 claims abstract description 8
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 20
- 239000007789 gas Substances 0.000 claims description 20
- 239000002826 coolant Substances 0.000 claims description 19
- 230000000712 assembly Effects 0.000 claims description 16
- 238000000429 assembly Methods 0.000 claims description 16
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 10
- 229910052786 argon Inorganic materials 0.000 claims description 10
- 229910052708 sodium Inorganic materials 0.000 claims description 10
- 239000011734 sodium Substances 0.000 claims description 10
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 7
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims description 7
- 229910052753 mercury Inorganic materials 0.000 claims description 7
- 239000000356 contaminant Substances 0.000 claims description 6
- 150000001247 metal acetylides Chemical class 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 230000001627 detrimental effect Effects 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 238000011084 recovery Methods 0.000 claims 1
- 230000003252 repetitive effect Effects 0.000 abstract 1
- 238000005253 cladding Methods 0.000 description 5
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 5
- 229910052778 Plutonium Inorganic materials 0.000 description 4
- 229910052770 Uranium Inorganic materials 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- OYEHPCDNVJXUIW-UHFFFAOYSA-N plutonium atom Chemical compound [Pu] OYEHPCDNVJXUIW-UHFFFAOYSA-N 0.000 description 4
- 238000004891 communication Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 238000009489 vacuum treatment Methods 0.000 description 2
- 229910001066 Pu alloy Inorganic materials 0.000 description 1
- 229910000711 U alloy Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002925 low-level radioactive waste Substances 0.000 description 1
- 239000003758 nuclear fuel Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- BITYAPCSNKJESK-UHFFFAOYSA-N potassiosodium Chemical compound [Na].[K] BITYAPCSNKJESK-UHFFFAOYSA-N 0.000 description 1
- 239000012857 radioactive material Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 210000000352 storage cell Anatomy 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- G21F9/001—Decontamination of contaminated objects, apparatus, clothes, food; Preventing contamination thereof
Definitions
- the present invention broadly relates to a method of cleaning a spent fuel assembly which has been removed from service in a nuclear reactor. It particularly relates to a method of cleaning such a spent fuel assembly contaminated with a radioactive alkali metal and in which the fuel assembly comprises a spent fissile material selected from the group consisting of oxides and carbides of uranium and/or plutonium or a metallic uranium/plutonium alloy.
- the typical breeder reactor utilizes an alkali metal as a coolant.
- a primary coolant is circulated via a pump through a core of fuel assemblies and then through a heat exchanger from which thermal energy is extracted by indirect heat exchange with a secondary coolant.
- the primary coolant picks up a certain amount of radioactivity in passing through the core. All components in contact with this primary coolant also become contaminated with the radioactive constituents. Thus, any component in contact with such coolant after removal from service must be cleaned, not only to remove the highly reactive coolant but also the radioactive contaminants.
- One method utilized for cleaning such components is to wash them with an organic solvent such as alcohol or wash them with water.
- the disadvantage of these methods is that they produce a large volume of liquid, low-level radioactive waste with its attendant storage and disposal problems.
- Another technique utilized is to heat the contaminated parts to a sufficient temperature to volatilize the alkali metal and the radioactive constituents.
- a fuel assembly removed from a breeder reactor presents a particularly unique problem.
- the cladding of some of the individual fuel pins comprising the fuel assembly could have been cracked or ruptured such that some of the alkali metal will be within the cladding of the individual pins.
- the spent fuel assembly after removal from service, will continue to generate some heat generally referred to as decay heat.
- the individual pins could generate sufficient heat to rupture the cladding of those pins which were still intact with the release of more radioactive material.
- the use of external heating would be equally inapplicable. Obviously there is a need for a procedure uniquely adapted to the cleaning of a spent fuel assembly which has been in contact with an alkali metal coolant.
- Still another object of the invention is to provide such a method which also produces an offgas stream free of alkali metal and radioactive contaminants such that the offgas may be reused for additional cleaning.
- the present invention provides a method of decontaminating a fuel assembly contaminated with a radioactive alkali metal.
- a fuel assembly comprises a plurality of elongated metal pins or tubes containing a spent fissile material.
- the present invention is particularly suitable for fuel assemblies containing a fissile material selected from the group consisting of carbides and oxides of uranium and/or plutonium and which are going to be reprocessed.
- the method comprises a plurality of sequential steps. First, the fuel assembly is placed in a sealed chamber. A heated inert gas is passed through the chamber to heat the fuel assembly to a temperature sufficient to cause evaporation of the alkali metal but not so high as to affect the structural integrity of the individual metal pins.
- the chamber is evacuated to a pressure of about less than 0.05 and preferably less than 0.005 mm of mercury and maintained at that pressure until the temperature of the fuel assembly increases to a level which could affect the structural integrity of the metal pin, typically about 1000°F.
- a cool, inert gas is introduced through the chamber and the fuel assemblies to reduce the temperature of the fuel assembly back to a safe level, typically about 800°F.
- the vacuum and cooling steps are repeated as often as required to insure removal of substantially all of the radioactive alkali metal.
- the decontaminated fuel assemblies may then be removed from the chamber and are suitable for shipment to a chemical reprocessing center.
- the inert gas utilized is argon and the gases removed from the sealed chamber are passed in indirect heat exchange relationship with a coolant for the condensation and removal of any vaporized alkali metal contained therein.
- the coolant will be one which is inert with respect to the alkali metal, for example, alcohol or other organic liquids.
- the gas removed from the chamber when it is being evacuated is also passed through a cryogenic trap to insure substantially complete removal of any remaining radioactive alkali metal from the gas.
- the alkali metal will be either sodium or a mixture of sodium and potassium.
- the method of the present invention is particularly applicable for use in a fuel storage building which is maintained in an inert atmosphere and generally is located adjacent the reactor from which the fuel assemblies are removed.
- the inert gas within the facility may be used for the heating and cooling, and after treatment for removal of sodium or other alkali metal, may be introduced into an existing gas cleaning facility which is provided within such storage buildings.
- the sole figure is a schematic of an arrangement of apparatus for use in the practice of the present invention.
- the present invention provides a method of decontaminating fuel assemblies which is uniquely suited for fuel assemblies removed from a breeder reactor.
- a coolant typically sodium potassium or a mixture thereof
- the reactor core comprises an array of fuel assemblies provided with passageways for the circulation of the coolant therethrough.
- Each fuel assembly is in turn comprised of a plurality of fuel pins.
- the fuel pin typically is an elongated, stainless steel cylinder or tube which is sealed at each end and contains, throughout a substantial portion of its length, fuel pellets.
- the outer metal portion of the pin generally is referred to as the cladding.
- the fuel pellet is formed from an oxide or carbide of uranium and/or plutonium, some of the uranium may be converted to plutonium during service as a result of exposure to the fast neutrons.
- breeder reactor facilities include an adjacent fuel storage building which is maintained under an inert atmosphere, typically argon gas. New fuel assemblies for loading in the reactor as well as spent fuel assemblies removed from the reactor, are temporarily stored in such a facility. It is an advantage of the present invention that it is particularly suited for use in such an environment.
- the apparatus includes a sealed chamber 12 for containing a spent fuel assembly 14.
- Fuel assembly 14 rests on a baffle member 16 and extends therethrough.
- Baffle member 16 engages the outer periphery of fuel assembly 14 to insure that those gases entering an upper portion 18 of chamber 12 must flow through fuel assembly 14 and into a lower portion 20 of chamber 12.
- Lower portion 20 of chamber 12 is provided with a recirculation outlet conduit 24 which is in fluid communication with a blower 26 which discharges into a recirculation inlet conduit 28 which is located above baffle member 16.
- conduit 28 also is provided with an electrical heater 30.
- Blower 26 is driven by a motor 32 which is interconnected to blower 26 via a magnetic coupling 34. Typically there also will be provided some means for preventing the transfer of heat from blower 26 back to magnetic coupling 34. As depicted, this would be accomplished by a cooling jacket 36 provided with an inlet and outlet for the flow of a cooling fluid therethrough.
- Chamber 12 also includes a conduit 38 and valve 40 for the introduction of an inert gas into chamber 12 in upper portion 18. Any inert gas may be used, typically the inert gas will be argon, particularly when the method of the present invention is practiced within a fuel storage cell which is maintained under an inert atmosphere of argon.
- An upper end of chamber 12 is provided with a discharge conduit 42 for conducting gas exiting upper portion 18 of chamber 12 to a condenser 44.
- Condenser 44 includes means for passing a coolant through an internal cooling coil 46 to condense any sodium vapors contained in the gas passing therethrough. Generally the coolant will be an organic fluid which is inert with respect to the alkali metal to prevent any reaction in the event of a leak.
- Condenser 44 further includes a sump portion 48 for the collection of condensed alkali metal coolant.
- a conduit 50 provides fluid communication between condenser 48 and a cryogenic trap 52 and also a bypass conduit 54.
- cryogenic trap 52 Downstream of cryogenic trap 52 are two vacuum pumps 56 and 58. Pumps 56 and 58 are in fluid communication with cryogenic trap 52 via conduits and valves 60,61 and 62. Pump 58 is also provided with a discharge conduit 64.
- a fuel assembly 14 is placed within chamber 12 which is then sealed.
- An inert gas typically argon, is introduced into chamber 12 through conduit 38 and valve 40.
- spent fuel assembly 14 will have an initial temperature of about 400°F (204°C).
- Power is supplied to motor 32 which drives blower 26 via magnetic coupling 34 to cause circulation of the argon from lower portion 20 of chamber 12 through conduit 24 and back to upper portion 18 of chamber 12 via conduit 28. Power also is supplied to electric heater 30 until the temperature of the fuel assembly is increased to about 800°F.
- vacuum pump 58 will be a dry, reciprocating vacuum pump which is operated for a sufficient time to decrease the chamber pressure from atmospheric to approximately 10 mm of mercury, during which time blower 26 is maintained in operation.
- secondary vacuum pump 56 typically an oil-sealed rotary pump
- Valves 52 and 62 are opened and 61 closed.
- the chamber pressure is then further decreased from 10 mm of mercury to at least .05 mm of mercury.
- the secondary vacuum pump 56 is operated until the pressure within chamber 12 is reduced to 0.005 mm of mercury or less. During this time, blower 26 is inoperative.
- the gas and entrained sodium vapor is withdrawn via conduit 42 and cooled in condenser 44. Any residual sodium vapor leaving through conduit 50 is removed in cryogenic trap 52.
- the condensed sodium may be recovered at a later point in time. Typically, this would be accomplished in condenser 44, for example, by increasing the coolant temperature to melt the sodium and then draining it from sump 48.
- the fuel assembly temperature will continue to increase as a result of the decay heat. When the temperature reaches the maximum safe temperature for the cladding of the individual fuel pins, generally about 1000°F, the vacuum treatment is stopped.
- Valves 60, 61 and 62 are closed and pumps 56 and 58 turned off.
- Valve 40 is open and chamber 12 is filled with argon gas to one atmosphere via conduit 38. After chamber 12 is filled with gas, valve 40 is closed and valve 55 opened. Power is supplied to motor 32 to drive blower 26 and the majority of the argon gas is circulated through valve 55 and conduit 54 in a reverse direction through condenser 44 and back to chamber 12 via conduit 42. The cause of the reverse circulation is the backpressure created by the presence of heater 30 in conduit 28.
- a valve could be provided in conduit 28 downstream of heater 30 to ensure that all of the gas circulated through conduit 54.
- the gas is circulated through chamber 12 and fuel assembly 14 until the temperature of the fuel assembly is reduced back to a desired level, typically below 800°F.
- the vacuum treatment and cooling are repeated as required to insure substantially complete removal of the radioactive alkali metal contaminant.
- the number of cycles required is readily determinable through experimentation. It will be appreciated that various other valves and instrumentation such as pressure sensors, temperature sensors, also would normally be incorporated as well as additional redundant gas cleaning techniques. However, those matters are well within the skill of those versed in the art.
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Food Science & Technology (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Cleaning In General (AREA)
Abstract
Description
- The present invention broadly relates to a method of cleaning a spent fuel assembly which has been removed from service in a nuclear reactor. It particularly relates to a method of cleaning such a spent fuel assembly contaminated with a radioactive alkali metal and in which the fuel assembly comprises a spent fissile material selected from the group consisting of oxides and carbides of uranium and/or plutonium or a metallic uranium/plutonium alloy.
- The typical breeder reactor utilizes an alkali metal as a coolant. In operation of the reactor a primary coolant is circulated via a pump through a core of fuel assemblies and then through a heat exchanger from which thermal energy is extracted by indirect heat exchange with a secondary coolant. The primary coolant picks up a certain amount of radioactivity in passing through the core. All components in contact with this primary coolant also become contaminated with the radioactive constituents. Thus, any component in contact with such coolant after removal from service must be cleaned, not only to remove the highly reactive coolant but also the radioactive contaminants.
- One method utilized for cleaning such components is to wash them with an organic solvent such as alcohol or wash them with water. The disadvantage of these methods is that they produce a large volume of liquid, low-level radioactive waste with its attendant storage and disposal problems.
- Another technique utilized is to heat the contaminated parts to a sufficient temperature to volatilize the alkali metal and the radioactive constituents.
- It also has been proposed to place such contaminated components in a chamber maintained under a vacuum to remove alkali metal vapors and radioactive constituents.
- A fuel assembly removed from a breeder reactor presents a particularly unique problem. For example, during service the cladding of some of the individual fuel pins comprising the fuel assembly could have been cracked or ruptured such that some of the alkali metal will be within the cladding of the individual pins. In addition, the spent fuel assembly, after removal from service, will continue to generate some heat generally referred to as decay heat. Thus, if the fuel assembly was placed in a vacuum the individual pins could generate sufficient heat to rupture the cladding of those pins which were still intact with the release of more radioactive material. Clearly, the use of external heating would be equally inapplicable. Obviously there is a need for a procedure uniquely adapted to the cleaning of a spent fuel assembly which has been in contact with an alkali metal coolant.
- It is an object of the invention to provide a cleaning and decontamination method particularly adapted for cleaning spent fuel assemblies.
- It is another object of the invention to provide a method for cleaning such fuel assemblies which is both economical and efficient in removing contaminants.
- It is another object of the invention to provide such a cleaning method which can accommodate increases in temperature resulting from decay heat of the fuel assemblies.
- It is another object of the invention to provide a fuel assembly cleaning method which utilizes a combination of heat and vacuum.
- Still another object of the invention is to provide such a method which also produces an offgas stream free of alkali metal and radioactive contaminants such that the offgas may be reused for additional cleaning.
- These and other objects of the invention will be more apparent from the drawing and following detailed description thereof.
- The present invention provides a method of decontaminating a fuel assembly contaminated with a radioactive alkali metal. Typically, a fuel assembly comprises a plurality of elongated metal pins or tubes containing a spent fissile material. The present invention is particularly suitable for fuel assemblies containing a fissile material selected from the group consisting of carbides and oxides of uranium and/or plutonium and which are going to be reprocessed. The method comprises a plurality of sequential steps. First, the fuel assembly is placed in a sealed chamber. A heated inert gas is passed through the chamber to heat the fuel assembly to a temperature sufficient to cause evaporation of the alkali metal but not so high as to affect the structural integrity of the individual metal pins. Thereafter the chamber is evacuated to a pressure of about less than 0.05 and preferably less than 0.005 mm of mercury and maintained at that pressure until the temperature of the fuel assembly increases to a level which could affect the structural integrity of the metal pin, typically about 1000°F. At that time a cool, inert gas is introduced through the chamber and the fuel assemblies to reduce the temperature of the fuel assembly back to a safe level, typically about 800°F. The vacuum and cooling steps are repeated as often as required to insure removal of substantially all of the radioactive alkali metal. The decontaminated fuel assemblies may then be removed from the chamber and are suitable for shipment to a chemical reprocessing center.
- In accordance with certain preferred embodiments of the invention the inert gas utilized is argon and the gases removed from the sealed chamber are passed in indirect heat exchange relationship with a coolant for the condensation and removal of any vaporized alkali metal contained therein. Typically, the coolant will be one which is inert with respect to the alkali metal, for example, alcohol or other organic liquids.
- In accordance with another preferred embodiment, the gas removed from the chamber when it is being evacuated is also passed through a cryogenic trap to insure substantially complete removal of any remaining radioactive alkali metal from the gas. Typically, the alkali metal will be either sodium or a mixture of sodium and potassium.
- The method of the present invention is particularly applicable for use in a fuel storage building which is maintained in an inert atmosphere and generally is located adjacent the reactor from which the fuel assemblies are removed. In such application the inert gas within the facility may be used for the heating and cooling, and after treatment for removal of sodium or other alkali metal, may be introduced into an existing gas cleaning facility which is provided within such storage buildings.
- The sole figure is a schematic of an arrangement of apparatus for use in the practice of the present invention.
- The present invention provides a method of decontaminating fuel assemblies which is uniquely suited for fuel assemblies removed from a breeder reactor. In a breeder reactor, a coolant, typically sodium potassium or a mixture thereof, is circulated through a reactor core wherein it is heated and subsequently the heat is extracted from the coolant. The reactor core comprises an array of fuel assemblies provided with passageways for the circulation of the coolant therethrough. Each fuel assembly is in turn comprised of a plurality of fuel pins. The fuel pin typically is an elongated, stainless steel cylinder or tube which is sealed at each end and contains, throughout a substantial portion of its length, fuel pellets. The outer metal portion of the pin generally is referred to as the cladding. Generally, the fuel pellet is formed from an oxide or carbide of uranium and/or plutonium, some of the uranium may be converted to plutonium during service as a result of exposure to the fast neutrons.
- During service, it is not uncommon for an individual fuel pin to crack or rupture such that the alkali metal coolant seeps within the metal tube. This. of course, complicates cleaning. To reprocess the fuel from a breeder reactor, it is essential that all of the alkali metal be removed as it will have a detrimental effect on the subsequent chemical reprocessing. In addition, during service, the alkali metal picks up radioactive contaminants which if not removed could complicate the handling and shipment of the fuel assemblies.
- Generally, breeder reactor facilities include an adjacent fuel storage building which is maintained under an inert atmosphere, typically argon gas. New fuel assemblies for loading in the reactor as well as spent fuel assemblies removed from the reactor, are temporarily stored in such a facility. It is an advantage of the present invention that it is particularly suited for use in such an environment.
- Referring now to the drawing, therein is depicted an arrangement of
apparatus 10 for use in practicing the method of the present invention. The apparatus includes a sealedchamber 12 for containing aspent fuel assembly 14.Fuel assembly 14 rests on abaffle member 16 and extends therethrough. Bafflemember 16 engages the outer periphery offuel assembly 14 to insure that those gases entering anupper portion 18 ofchamber 12 must flow throughfuel assembly 14 and into alower portion 20 ofchamber 12.Lower portion 20 ofchamber 12 is provided with arecirculation outlet conduit 24 which is in fluid communication with ablower 26 which discharges into arecirculation inlet conduit 28 which is located abovebaffle member 16. Advantageously,conduit 28 also is provided with anelectrical heater 30. Blower 26 is driven by amotor 32 which is interconnected to blower 26 via amagnetic coupling 34. Typically there also will be provided some means for preventing the transfer of heat fromblower 26 back tomagnetic coupling 34. As depicted, this would be accomplished by a coolingjacket 36 provided with an inlet and outlet for the flow of a cooling fluid therethrough. -
Chamber 12 also includes a conduit 38 andvalve 40 for the introduction of an inert gas intochamber 12 inupper portion 18. Any inert gas may be used, typically the inert gas will be argon, particularly when the method of the present invention is practiced within a fuel storage cell which is maintained under an inert atmosphere of argon. An upper end ofchamber 12 is provided with adischarge conduit 42 for conducting gas exitingupper portion 18 ofchamber 12 to acondenser 44.Condenser 44 includes means for passing a coolant through aninternal cooling coil 46 to condense any sodium vapors contained in the gas passing therethrough. Generally the coolant will be an organic fluid which is inert with respect to the alkali metal to prevent any reaction in the event of a leak.Condenser 44 further includes asump portion 48 for the collection of condensed alkali metal coolant. Aconduit 50 provides fluid communication betweencondenser 48 and acryogenic trap 52 and also abypass conduit 54. - Downstream of
cryogenic trap 52 are twovacuum pumps Pumps cryogenic trap 52 via conduits andvalves Pump 58 is also provided with adischarge conduit 64. - In accordance with the practice of the method of the present invention, a
fuel assembly 14 is placed withinchamber 12 which is then sealed. An inert gas, typically argon, is introduced intochamber 12 through conduit 38 andvalve 40. Generally, spentfuel assembly 14 will have an initial temperature of about 400°F (204°C). - Power is supplied to
motor 32 which drivesblower 26 viamagnetic coupling 34 to cause circulation of the argon fromlower portion 20 ofchamber 12 throughconduit 24 and back toupper portion 18 ofchamber 12 viaconduit 28. Power also is supplied toelectric heater 30 until the temperature of the fuel assembly is increased to about 800°F. - After the fuel assembly has been heated to a desired temperature, power to the electric heater is turned off,
valve 61 is opened andvacuum pump 58 started. Typically,vacuum pump 58 will be a dry, reciprocating vacuum pump which is operated for a sufficient time to decrease the chamber pressure from atmospheric to approximately 10 mm of mercury, during whichtime blower 26 is maintained in operation. Thereafter, secondary vacuum pump 56 (typically an oil-sealed rotary pump) is started.Valves secondary vacuum pump 56 is operated until the pressure withinchamber 12 is reduced to 0.005 mm of mercury or less. During this time,blower 26 is inoperative. - During the vacuum drying time, the gas and entrained sodium vapor is withdrawn via
conduit 42 and cooled incondenser 44. Any residual sodium vapor leaving throughconduit 50 is removed incryogenic trap 52. The condensed sodium may be recovered at a later point in time. Typically, this would be accomplished incondenser 44, for example, by increasing the coolant temperature to melt the sodium and then draining it fromsump 48. During the vacuum drying time, the fuel assembly temperature will continue to increase as a result of the decay heat. When the temperature reaches the maximum safe temperature for the cladding of the individual fuel pins, generally about 1000°F, the vacuum treatment is stopped. -
Valves Valve 40 is open andchamber 12 is filled with argon gas to one atmosphere via conduit 38. Afterchamber 12 is filled with gas,valve 40 is closed andvalve 55 opened. Power is supplied tomotor 32 to driveblower 26 and the majority of the argon gas is circulated throughvalve 55 andconduit 54 in a reverse direction throughcondenser 44 and back tochamber 12 viaconduit 42. The cause of the reverse circulation is the backpressure created by the presence ofheater 30 inconduit 28. Alternatively, of course, a valve could be provided inconduit 28 downstream ofheater 30 to ensure that all of the gas circulated throughconduit 54. The gas is circulated throughchamber 12 andfuel assembly 14 until the temperature of the fuel assembly is reduced back to a desired level, typically below 800°F. The vacuum treatment and cooling are repeated as required to insure substantially complete removal of the radioactive alkali metal contaminant. The number of cycles required is readily determinable through experimentation. It will be appreciated that various other valves and instrumentation such as pressure sensors, temperature sensors, also would normally be incorporated as well as additional redundant gas cleaning techniques. However, those matters are well within the skill of those versed in the art. - The foregoing description and example illustrate a specific embodiment of the invention and what is now considered to be the best mode of practicing it. Those skilled in the art, however, will understand that changes may be made in the form of the invention without departing from its generally broad scope. Accordingly, it should be understood that within the scope of the appended claims the invention may be practiced otherwise than as is specifically illustrated and described.
- What is claimed and desired to be secured by Letters Patent of the United States is:
Claims (9)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US2332187A | 1987-03-09 | 1987-03-09 | |
US23321 | 1987-03-09 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0281680A1 true EP0281680A1 (en) | 1988-09-14 |
EP0281680B1 EP0281680B1 (en) | 1992-03-11 |
Family
ID=21814411
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19870118413 Expired EP0281680B1 (en) | 1987-03-09 | 1987-12-11 | Method of cleaning a spent fuel assembly |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0281680B1 (en) |
JP (1) | JPS63235900A (en) |
DE (1) | DE3777392D1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2803083A1 (en) * | 1999-12-24 | 2001-06-29 | Framatome Sa | Water-cooled nuclear reactor fuel assembly cleaning comprises moving assembly vertically through suction housing in pond and agitating water |
CN102077300B (en) * | 2008-06-25 | 2014-04-23 | 原子能与可替代能源委员会 | Method of treating a structure containing sodium and a radioactive substance |
US8850715B2 (en) * | 2006-09-07 | 2014-10-07 | Eisenmann Ag | Process and installation for drying articles |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09178895A (en) * | 1996-04-09 | 1997-07-11 | Kawasaki Heavy Ind Ltd | Sodium removing equipment for fast reactor core constituting element |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2394871A1 (en) * | 1977-06-16 | 1979-01-12 | Interatom | ELIMINATION BY DISTILLATION OF THE LIQUID METAL ADHESIVE TO THE CORE ELEMENTS OF REACTORS |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63186195A (en) * | 1987-01-27 | 1988-08-01 | 三菱原子力工業株式会社 | Spent core constituent washer |
-
1987
- 1987-12-11 DE DE8787118413T patent/DE3777392D1/en not_active Expired - Fee Related
- 1987-12-11 EP EP19870118413 patent/EP0281680B1/en not_active Expired
-
1988
- 1988-03-09 JP JP5385188A patent/JPS63235900A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2394871A1 (en) * | 1977-06-16 | 1979-01-12 | Interatom | ELIMINATION BY DISTILLATION OF THE LIQUID METAL ADHESIVE TO THE CORE ELEMENTS OF REACTORS |
Non-Patent Citations (1)
Title |
---|
CHEMICAL ABSTRACTS, vol. 95, 1981, page 219, abstract no. 190592b, Columbus, Ohio, US; & JP-A-56 087 637 (MITSUBISHI HEAVY INDUSTRIES, LTD.) 16-07-1981 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2803083A1 (en) * | 1999-12-24 | 2001-06-29 | Framatome Sa | Water-cooled nuclear reactor fuel assembly cleaning comprises moving assembly vertically through suction housing in pond and agitating water |
WO2001048760A1 (en) * | 1999-12-24 | 2001-07-05 | Framatome Anp | Method and device for cleaning a nuclear reactor fuel assembly |
US8850715B2 (en) * | 2006-09-07 | 2014-10-07 | Eisenmann Ag | Process and installation for drying articles |
CN102077300B (en) * | 2008-06-25 | 2014-04-23 | 原子能与可替代能源委员会 | Method of treating a structure containing sodium and a radioactive substance |
Also Published As
Publication number | Publication date |
---|---|
JPS63235900A (en) | 1988-09-30 |
EP0281680B1 (en) | 1992-03-11 |
DE3777392D1 (en) | 1992-04-16 |
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