CA1099089A - Nuclear fuel recycling system - Google Patents
Nuclear fuel recycling systemInfo
- Publication number
- CA1099089A CA1099089A CA314,385A CA314385A CA1099089A CA 1099089 A CA1099089 A CA 1099089A CA 314385 A CA314385 A CA 314385A CA 1099089 A CA1099089 A CA 1099089A
- Authority
- CA
- Canada
- Prior art keywords
- slurry
- pellets
- powder
- grinding
- nuclear fuel
- 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.)
- Expired
Links
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C3/00—Reactor fuel elements and their assemblies; Selection of substances for use as reactor fuel elements
- G21C3/42—Selection of substances for use as reactor fuel
- G21C3/58—Solid reactor fuel Pellets made of fissile material
- G21C3/62—Ceramic fuel
- G21C3/623—Oxide fuels
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical & Material Sciences (AREA)
- Ceramic Engineering (AREA)
- Plasma & Fusion (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
In the processes of nuclear fuel manufacture, scrap material such as uncontaminated reject powder and reject pellets, which would previously have been reprocessed chemically in conversion of the uranium values by dissolution into liquid form, is now mechanically reduced by crushing in a substantially inert atmosphere and converted to a slurry having between about 70 to 85 weight per cent solids, and then attrition milled utilizing scrap sintered UO2 pellets as the reducing medium. Grinding swarf generated during the centreless grinding of UO2 pellets may also be recycled provided it is sufficiently pure.
In the processes of nuclear fuel manufacture, scrap material such as uncontaminated reject powder and reject pellets, which would previously have been reprocessed chemically in conversion of the uranium values by dissolution into liquid form, is now mechanically reduced by crushing in a substantially inert atmosphere and converted to a slurry having between about 70 to 85 weight per cent solids, and then attrition milled utilizing scrap sintered UO2 pellets as the reducing medium. Grinding swarf generated during the centreless grinding of UO2 pellets may also be recycled provided it is sufficiently pure.
Description
~ 9 Case 2570 This invention is directed to a method of recycling scrap nuclear material, and nuclear fuel manufactured by the process.
In the manufacture of nuclear fuel for use in nuclear reactors, the conditions of service to which the fuel is subject within a reactor are so demanding that very high manufacturing standards must be met, which leads to a comparatively high volume of reject sintered pellet material, and the need for recycling this reject fuel material. In addition to pelleted material, the swarf resulting from pellet grinding also requires to be recycled. At present sueh nuclear fuel reeyeling generally relies upon ehemieal dissolution of uranium values into liquid form followed by purifieation, preeipitation and eventual powder manufaeture.
In aecordanee with the present invention, suitable serap material may be prepared meehanieally by erushing and milling as a high solids eontent slurry, using serap sintered UO2 pellets as the grinding medium, to provide powder of aeeeptable density and purity for reeyeling in a pellet produetion line. In order to optimize utilization of the present fuel serap retrieval system, the grinding wheels used in initially grinding sintered pellets require to be sueh that they do not introduee eontamination - into the proeess (e.g. use of diamond wheels) in order to maintain the purity of the ensuing grinding swarf, for retrieval through the subjeet meehanieal proeess.
The use of UO2 sintered balls as the grinding media is shown in Canadian Patent No. 656,281, Moss, dated January 22, 1963.
Thus there is provided a method of produeing nuelear fuel from retrieved nuelear fuel material of high Case 2570 purity selected from the group comprising substantially uncontaminated grinding swarf and powder and pelleted fuel, including the steps of:
(1) crushing scrap pellets to a fine powder
In the manufacture of nuclear fuel for use in nuclear reactors, the conditions of service to which the fuel is subject within a reactor are so demanding that very high manufacturing standards must be met, which leads to a comparatively high volume of reject sintered pellet material, and the need for recycling this reject fuel material. In addition to pelleted material, the swarf resulting from pellet grinding also requires to be recycled. At present sueh nuclear fuel reeyeling generally relies upon ehemieal dissolution of uranium values into liquid form followed by purifieation, preeipitation and eventual powder manufaeture.
In aecordanee with the present invention, suitable serap material may be prepared meehanieally by erushing and milling as a high solids eontent slurry, using serap sintered UO2 pellets as the grinding medium, to provide powder of aeeeptable density and purity for reeyeling in a pellet produetion line. In order to optimize utilization of the present fuel serap retrieval system, the grinding wheels used in initially grinding sintered pellets require to be sueh that they do not introduee eontamination - into the proeess (e.g. use of diamond wheels) in order to maintain the purity of the ensuing grinding swarf, for retrieval through the subjeet meehanieal proeess.
The use of UO2 sintered balls as the grinding media is shown in Canadian Patent No. 656,281, Moss, dated January 22, 1963.
Thus there is provided a method of produeing nuelear fuel from retrieved nuelear fuel material of high Case 2570 purity selected from the group comprising substantially uncontaminated grinding swarf and powder and pelleted fuel, including the steps of:
(1) crushing scrap pellets to a fine powder
(2) mixing with grinding swarf and clean and virgin powder, and adding liquid to form a slurry having a density in the range 70 to 85 weight per cent solids;
(3) adding sintered UO2 pellets as grinding media, to the slurry in an attrition mill, and
(4) grinding the slurry and pellets in the mill to a predetermined consistency.
The process can include green pellet forms in the material being treated.
The resulting ground slurry is dried to a cake and granulated. The dried granulated powder is recycled to a fuel pelleting line in combination with virgin feed stock. The virgin feed stock is usually subjected to the milling process simultaneously with the recycled material.
In carrying out the initial step of crushing the scrap UO2 material which is highly oxidizable, the spraying of liquid nitrogen for purposes of providing an inert atmosphere also serves to reduce the temperature of the UO2 significantly, to increase its brittleness and reduce its reactivity, thereby significantly diminishing wear on the hammer mill while providing a substantially inert atmosphere.
The subject process offers large savings, both in avoidance of needless dissolution reprocessing, and in the fact that undue handling of reject nuclear fuel by shipping it to a distant dissolution plant is avoided, while the dried powder that the process yields is of 1~9~ Case 2570 excellent size distribution and purity for use in the pellet making process.
The step of pulverizing pelleted material can involve the use of jaw crushers and hammer mills in a suitably inert atmosphere, preferably using liquid nitrogen as referred to above, with unsintered (green) pellets being added at the hammer mill stage of reduction.
The starting materials of this process may include any of: grinding swarf, sintered scrap, green scrap and clean or virgin powder.
The sintered scrap is subject to a jaw crusher operation to reduce it to a powder. The powder then passes to a hammer mill, operated generally in a liquid nitrogen atmosphere to which any available green scrap (non-sintered) is added. Available grinding swarf in a substantially non-contaminated condition is added to the crushed material and the mixture passed to a wet mill utilizing reject sintered fuel pellets as the reducing media, the slurry having a high solids content, normally : 20 in the range 70 to 85 weight per cent solids, and including virgin fuel powder (UO2). The milled material is dried when a predetermined consistency has been achieved, and processed into pellets.
The virgin UO2 powder is normally added as a component of the slurry in the wet ball mill, so that when dried, the ball mill product is in a suitable condition for repelleting.
In the subject process, by selection of substantially uncontaminated materials, together with steps to substantially preclude oxidation of the material during processing, the need for chemical recycling can be avoided, in large measure, ~ Case 2570 and an end product of suitable purity and appropriate particle size distribution obtained, to facilitate repelleting.
Significant cost savings may be effected, both in handling and in transportation, while the nuclear fuel inventory also is reduced, with commensurate savings.
The process can include green pellet forms in the material being treated.
The resulting ground slurry is dried to a cake and granulated. The dried granulated powder is recycled to a fuel pelleting line in combination with virgin feed stock. The virgin feed stock is usually subjected to the milling process simultaneously with the recycled material.
In carrying out the initial step of crushing the scrap UO2 material which is highly oxidizable, the spraying of liquid nitrogen for purposes of providing an inert atmosphere also serves to reduce the temperature of the UO2 significantly, to increase its brittleness and reduce its reactivity, thereby significantly diminishing wear on the hammer mill while providing a substantially inert atmosphere.
The subject process offers large savings, both in avoidance of needless dissolution reprocessing, and in the fact that undue handling of reject nuclear fuel by shipping it to a distant dissolution plant is avoided, while the dried powder that the process yields is of 1~9~ Case 2570 excellent size distribution and purity for use in the pellet making process.
The step of pulverizing pelleted material can involve the use of jaw crushers and hammer mills in a suitably inert atmosphere, preferably using liquid nitrogen as referred to above, with unsintered (green) pellets being added at the hammer mill stage of reduction.
The starting materials of this process may include any of: grinding swarf, sintered scrap, green scrap and clean or virgin powder.
The sintered scrap is subject to a jaw crusher operation to reduce it to a powder. The powder then passes to a hammer mill, operated generally in a liquid nitrogen atmosphere to which any available green scrap (non-sintered) is added. Available grinding swarf in a substantially non-contaminated condition is added to the crushed material and the mixture passed to a wet mill utilizing reject sintered fuel pellets as the reducing media, the slurry having a high solids content, normally : 20 in the range 70 to 85 weight per cent solids, and including virgin fuel powder (UO2). The milled material is dried when a predetermined consistency has been achieved, and processed into pellets.
The virgin UO2 powder is normally added as a component of the slurry in the wet ball mill, so that when dried, the ball mill product is in a suitable condition for repelleting.
In the subject process, by selection of substantially uncontaminated materials, together with steps to substantially preclude oxidation of the material during processing, the need for chemical recycling can be avoided, in large measure, ~ Case 2570 and an end product of suitable purity and appropriate particle size distribution obtained, to facilitate repelleting.
Significant cost savings may be effected, both in handling and in transportation, while the nuclear fuel inventory also is reduced, with commensurate savings.
Claims (6)
1. The method of producing nuclear fuel comprising retrieved nuclear fuel material selected from the group comprising substantially uncontaminated grinding swarf, sintered pellets and green pellet forms, including the steps of:
(1) crushing pelleted material to fine powder in a substantially inert atmosphere;
(2) mixing with grinding swarf and liquid to form a slurry having a content between about 70 to 85 weight per cent solids;
(3) adding sintered UO2 pellets as grinding media to the slurry within a wet mill and (4) wet grinding the slurry with the pellets in the wet mill, to a predetermined consistency.
(1) crushing pelleted material to fine powder in a substantially inert atmosphere;
(2) mixing with grinding swarf and liquid to form a slurry having a content between about 70 to 85 weight per cent solids;
(3) adding sintered UO2 pellets as grinding media to the slurry within a wet mill and (4) wet grinding the slurry with the pellets in the wet mill, to a predetermined consistency.
2. The method as claimed in Claim 1 including the steps of drying said ground slurry to a powder, and recycling the powder for manufacture to pellet form.
3. The method as claimed in Claim 1 or Claim 2, wherein said slurry solids content is about 85 weight per cent.
4. The method as claimed in Claim 1 wherein said slurry includes the addition of clean powder UO2.
5. The method as claimed in Claim 4 wherein said clean powder is virgin UO2.
6. The method as claimed in claim 1, wherein the first step includes adding liquid nitrogen during the crushing to provide an inert atmosphere, whereby the temperature of the material is significantly reduced, to provide enhanced crushing action.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA314,385A CA1099089A (en) | 1978-10-26 | 1978-10-26 | Nuclear fuel recycling system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA314,385A CA1099089A (en) | 1978-10-26 | 1978-10-26 | Nuclear fuel recycling system |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1099089A true CA1099089A (en) | 1981-04-14 |
Family
ID=4112705
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA314,385A Expired CA1099089A (en) | 1978-10-26 | 1978-10-26 | Nuclear fuel recycling system |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA1099089A (en) |
-
1978
- 1978-10-26 CA CA314,385A patent/CA1099089A/en not_active Expired
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Legal Events
Date | Code | Title | Description |
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MKEX | Expiry |