CN107845433B - A kind of MOX powder forming agent and lubricant adding method - Google Patents
A kind of MOX powder forming agent and lubricant adding method Download PDFInfo
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- CN107845433B CN107845433B CN201610834813.XA CN201610834813A CN107845433B CN 107845433 B CN107845433 B CN 107845433B CN 201610834813 A CN201610834813 A CN 201610834813A CN 107845433 B CN107845433 B CN 107845433B
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- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 16
- 239000000314 lubricant Substances 0.000 title claims abstract description 15
- 239000000843 powder Substances 0.000 title claims abstract description 14
- 238000000034 method Methods 0.000 title claims abstract description 12
- 239000002245 particle Substances 0.000 claims abstract description 42
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 9
- 239000012535 impurity Substances 0.000 claims abstract description 7
- 238000002844 melting Methods 0.000 claims abstract description 7
- 230000008018 melting Effects 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 239000000498 cooling water Substances 0.000 claims abstract description 6
- 239000011701 zinc Substances 0.000 claims abstract description 6
- 238000012216 screening Methods 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical group [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 3
- 239000008116 calcium stearate Substances 0.000 claims description 3
- 235000013539 calcium stearate Nutrition 0.000 claims description 3
- 235000021588 free fatty acids Nutrition 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- FSWZDJUNHJMBSQ-UHFFFAOYSA-N lithium;octadecanoic acid Chemical group [Li].CCCCCCCCCCCCCCCCCC(O)=O FSWZDJUNHJMBSQ-UHFFFAOYSA-N 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 9
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052725 zinc Inorganic materials 0.000 abstract description 5
- 230000002159 abnormal effect Effects 0.000 abstract description 3
- 238000005054 agglomeration Methods 0.000 abstract description 3
- 230000002776 aggregation Effects 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000008187 granular material Substances 0.000 abstract 1
- LRXTYHSAJDENHV-UHFFFAOYSA-H zinc phosphate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LRXTYHSAJDENHV-UHFFFAOYSA-H 0.000 abstract 1
- 229910000165 zinc phosphate Inorganic materials 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- HGPXWXLYXNVULB-UHFFFAOYSA-M lithium stearate Chemical compound [Li+].CCCCCCCCCCCCCCCCCC([O-])=O HGPXWXLYXNVULB-UHFFFAOYSA-M 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
Classifications
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- 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
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- 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)
- Lubricants (AREA)
- Powder Metallurgy (AREA)
Abstract
一种MOX粉末成形剂与润滑剂添加方法,包括以下步骤:步骤一:选取硬质酸锌;步骤二:将硬质酸锌颗粒在15~40℃,真空度0.01~0.5Pa的条件下烘干0.5~3h,去除其中的挥发性杂质元素,并避免温度过高导致的颗粒异常增大现象以及熔化;步骤三:用20~100目的筛网对经步骤二处理的硬质酸锌颗粒进行筛分处理;步骤四:以15~35%的装填率计算所需的MOX颗粒量并加入到球磨罐中,将经步骤三处理的硬质酸锌颗粒以0.02~5.0%的重量比加入到MOX颗粒中,以5~15L/min的速度通入15~38℃的冷却水,避免因物料发热造成的团聚和熔化现象步骤五:用1~10r/min的速度混合5~45min,使硬质酸锌颗粒和MOX颗粒初步混合均匀,然后以1~20r/min的速度逐步增大混料机转速,在10~100r/min的速度下混合处理15~600min,避免剧烈混合导致的MOX颗粒破碎。A method for adding MOX powder forming agent and lubricant, comprising the following steps: step 1: selecting zinc stearate; step 2: drying zinc stearate particles at 15-40°C and vacuum degree of 0.01-0.5Pa Dry for 0.5-3 hours to remove the volatile impurity elements and avoid the abnormal growth and melting of particles caused by excessive temperature; Step 3: Use a 20-100 mesh screen to screen the zinc hardate particles treated in step 2 Screening treatment; Step 4: Calculate the required MOX particle amount with a filling rate of 15% to 35% and add it to the ball mill tank, and add the zinc stearate particles processed in step 3 to the In MOX granules, feed cooling water at 15-38°C at a speed of 5-15L/min to avoid agglomeration and melting caused by material heating. Step 5: Mix at a speed of 1-10r/min for 5-45min to make the hard Preliminarily mix zinc phosphate and MOX particles evenly, then gradually increase the speed of the mixer at a speed of 1-20r/min, and mix at a speed of 10-100r/min for 15-600min to avoid MOX particles caused by violent mixing broken.
Description
技术领域technical field
该技术属于成形剂与润滑剂添加领域,具体涉及一种MOX粉末成形剂与润滑剂添加方法。The technology belongs to the field of forming agent and lubricant addition, and specifically relates to a method for adding MOX powder forming agent and lubricant.
背景技术Background technique
MOX粉末细小,流动性较差,同时MOX芯块尺寸细小,并含有中心孔及倒角结构,因此,为了降低成型时粉末颗粒与模具壁和磨冲间的摩擦、改善生坯的密度分布、减少压模磨损和有利于脱模,应加入成形剂与润滑剂。The MOX powder is fine and has poor fluidity. At the same time, the MOX pellets are small in size and contain a central hole and a chamfer structure. Therefore, in order to reduce the friction between the powder particles and the mold wall and the grinding punch during molding, and improve the density distribution of the green body, To reduce die wear and facilitate demoulding, forming agents and lubricants should be added.
目前,传统行业的粉末成形剂与润滑剂添加技术主要存在五点不足,一是MOX物料会自发发热,而传统的成形剂在受热时容易熔化;二是MOX物料流动性较差,加入传统的成形剂时容易导致物料松装密度和流动性明显变差,对烧结体特性产生不利影响;三是MOX物料的核特性,不允许成形剂以溶液状态加入;四是传统的润滑剂添加技术是将润滑剂涂于模具内壁和压头上,考虑到MOX粉末的放射特性,这种人工涂抹润滑剂的方式不仅会增加人员的受辐照时间,同时也会降低生产效率;五是参数设置不合理导致MOX颗粒破碎等现象发生,影响物料的流动性和可压性。At present, there are five major deficiencies in the powder forming agent and lubricant adding technology in the traditional industry. First, MOX materials will spontaneously generate heat, while traditional forming agents are easy to melt when heated; second, MOX materials have poor fluidity. Forming agent will easily lead to obvious deterioration of bulk density and fluidity of the material, which will have an adverse effect on the characteristics of the sintered body; third, the nuclear characteristics of MOX materials do not allow the addition of forming agent in a solution state; fourth, the traditional lubricant addition technology is Apply lubricant to the inner wall of the mold and the pressure head. Considering the radiation characteristics of MOX powder, this method of manually applying lubricant will not only increase the irradiation time of personnel, but also reduce production efficiency; fifth, the parameters are not set properly. Reasonably lead to the occurrence of MOX particle breakage and other phenomena, affecting the fluidity and compressibility of materials.
发明内容Contents of the invention
本发明的目的在于:设计了一种MOX粉末成形剂与润滑剂添加方法,通过选择合适的成形剂,采用粉末润滑的方式,提高压坯强度,改善芯块制造的可靠性。The object of the present invention is to design a method for adding MOX powder forming agent and lubricant. By selecting a suitable forming agent and adopting powder lubrication, the strength of the green compact can be improved, and the reliability of pellet manufacturing can be improved.
本发明的技术方案如下:一种MOX粉末成形剂与润滑剂添加方法,包括以下步骤:The technical scheme of the present invention is as follows: a method for adding MOX powder forming agent and lubricant, comprising the following steps:
步骤一:选取硬质酸锌,其中硬质酸锌中金属锌含量10~11.2%,游离脂肪酸小于0.5%,水含量小于0.5%,粒度20~200目,选取MOX颗粒,粒度为185~500μm,比表面积为3~18m2/g,杂质含量为250~2600μg/g,松装密度为15~20%TD,填充率为78~80%,Carr流动性指数51~65,成型密度41~48%TD;Step 1: Select zinc stearate, wherein the metal zinc content in zinc stearate is 10-11.2%, the free fatty acid is less than 0.5%, the water content is less than 0.5%, the particle size is 20-200 mesh, and MOX particles are selected, the particle size is 185-500 μm , the specific surface area is 3~18m 2 /g, the impurity content is 250~2600μg/g, the bulk density is 15~20%TD, the filling rate is 78~80%, the Carr fluidity index is 51~65, and the molding density is 41~ 48%TD;
步骤二:将硬质酸锌颗粒在15~40℃,真空度0.01~0.5Pa的条件下烘干0.5~3h,去除其中的挥发性杂质元素,并避免温度过高导致的颗粒异常增大现象以及熔化;Step 2: Dry the zinc stearate particles at 15-40°C and a vacuum of 0.01-0.5Pa for 0.5-3 hours to remove volatile impurity elements and avoid abnormal particle growth caused by excessive temperature and melting;
步骤三:用20~100目的筛网对经步骤二处理的硬质酸锌颗粒进行筛分处理;Step 3: Screening the zinc hardate particles treated in step 2 with a 20-100 mesh screen;
步骤四:以15~35%的装填率计算所需的MOX颗粒量并加入到球磨罐中,将经步骤三处理的硬质酸锌颗粒以0.02~5.0%的重量比加入到MOX颗粒中,以5~15L/min的速度通入15~38℃的冷却水,避免因物料发热造成的团聚和熔化现象Step 4: Calculate the required amount of MOX particles with a filling rate of 15-35% and add them to the ball mill tank, and add the zinc stearate particles treated in step 3 to the MOX particles at a weight ratio of 0.02-5.0%, Inject cooling water at 15-38°C at a rate of 5-15L/min to avoid agglomeration and melting caused by heat generation of materials
步骤五:用1~10r/min的速度混合5~45min,使硬质酸锌颗粒和MOX颗粒初步混合均匀,然后以1~20r/min的速度逐步增大混料机转速,在10~100r/min的速度下混合处理15~600min,避免剧烈混合导致的MOX颗粒破碎。Step 5: Mix at a speed of 1 to 10r/min for 5 to 45 minutes to initially mix the zinc stearate particles and MOX particles evenly, and then gradually increase the speed of the mixer at a speed of 1 to 20r/min, at 10 to 100r Mix at a speed of 15-600min for 15-600min to avoid breakage of MOX particles caused by vigorous mixing.
还包括步骤六:以1~10r/min的速度逐步减小混料机转速直至停止,停止混合5~30min后,关闭冷却水。Step 6 is also included: gradually reduce the speed of the mixer at a speed of 1 to 10 r/min until it stops, and after stopping mixing for 5 to 30 minutes, turn off the cooling water.
所述步骤一中,硬质酸锌可用硬质酸钙或硬质酸锂代替。In said step one, zinc stearate can be replaced by calcium stearate or lithium stearate.
本发明的显著效果在于:有较好的粘结性和润滑性能,在混合粉末中容易均匀分散,且不发生化学变化;软化点温度高,混合时不易因温度升高而熔化;混合粉末中不至于因添加这些物质而使其松装密度和流动性明显变差,对烧结体特性也不会产生不利影响;加热时,从压坯中容易呈气体排出,并且这种气体不影响烧结炉寿命。The remarkable effects of the present invention are: good cohesiveness and lubricity, easy to disperse evenly in the mixed powder, and no chemical change; high softening point temperature, difficult to melt due to temperature rise during mixing; The bulk density and fluidity will not be significantly deteriorated due to the addition of these substances, and the properties of the sintered body will not be adversely affected; when heated, it is easy to discharge gas from the compact, and this gas does not affect the sintering furnace life.
具体实施方式Detailed ways
一种MOX粉末成形剂与润滑剂添加方法,包括以下步骤:A method for adding MOX powder forming agent and lubricant, comprising the following steps:
步骤一:选取硬质酸锌,其中硬质酸锌中金属锌含量10~11.2%,游离脂肪酸小于0.5%,水含量小于0.5%,粒度20~200目,选取MOX颗粒,粒度为185~500μm,比表面积为3~18m2/g,杂质含量为250~2600μg/g,松装密度为15~20%TD,填充率为78~80%,Carr流动性指数51~65,成型密度41~48%TD;硬质酸锌可用硬质酸钙或硬质酸锂代替;Step 1: Select zinc stearate, wherein the metal zinc content in zinc stearate is 10-11.2%, the free fatty acid is less than 0.5%, the water content is less than 0.5%, the particle size is 20-200 mesh, and MOX particles are selected, the particle size is 185-500 μm , the specific surface area is 3~18m 2 /g, the impurity content is 250~2600μg/g, the bulk density is 15~20%TD, the filling rate is 78~80%, the Carr fluidity index is 51~65, and the molding density is 41~ 48% TD; Zinc stearate can be replaced by calcium stearate or lithium stearate;
步骤二:将硬质酸锌颗粒在15~40℃,真空度0.01~0.5Pa的条件下烘干0.5~3h,去除其中的挥发性杂质元素,并避免温度过高导致的颗粒异常增大现象以及熔化;Step 2: Dry the zinc stearate particles at 15-40°C and a vacuum of 0.01-0.5Pa for 0.5-3 hours to remove volatile impurity elements and avoid abnormal particle growth caused by excessive temperature and melting;
步骤三:用20~100目的筛网对经步骤二处理的硬质酸锌颗粒进行筛分处理;Step 3: Screening the zinc hardate particles treated in step 2 with a 20-100 mesh screen;
步骤四:以15~35%的装填率计算所需的MOX颗粒量并加入到球磨罐中,将经步骤三处理的硬质酸锌颗粒以0.02~5.0%的重量比加入到MOX颗粒中,以5~15L/min的速度通入15~38℃的冷却水,避免因物料发热造成的团聚和熔化现象Step 4: Calculate the required amount of MOX particles with a filling rate of 15-35% and add them to the ball mill tank, and add the zinc stearate particles treated in step 3 to the MOX particles at a weight ratio of 0.02-5.0%, Cooling water at 15-38°C is introduced at a speed of 5-15L/min to avoid agglomeration and melting caused by heating of materials
步骤五:用1~10r/min的速度混合5~45min,使硬质酸锌颗粒和MOX颗粒初步混合均匀,然后以1~20r/min的速度逐步增大混料机转速,在10~100r/min的速度下混合处理15~600min,避免剧烈混合导致的MOX颗粒破碎Step 5: Mix at a speed of 1 to 10r/min for 5 to 45 minutes to initially mix the zinc stearate particles and MOX particles evenly, and then gradually increase the speed of the mixer at a speed of 1 to 20r/min, at 10 to 100r Mix at a speed of 15-600 minutes per minute to avoid broken MOX particles caused by vigorous mixing
步骤六:以1~10r/min的速度逐步减小混料机转速直至停止,停止混合5~30min后,关闭冷却水。Step 6: Gradually reduce the speed of the mixer at a speed of 1 to 10 r/min until it stops. After stopping mixing for 5 to 30 minutes, turn off the cooling water.
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| (U,Gd)O2可燃毒物芯块制造工艺及其主要性能;易伟等;《2004学术年会论文集》;20040501;第103-111页 * |
| CeO_2代替PuO_2模拟制造MOX燃料芯块的可行性;李怀林等;《原子能科学技术》;20030731;第37卷;第24-28页,第39页 * |
| mixed oxide fuel fabrication technology and experience at the belonucleaire and CFCa plants and further developments for the MELOX plant;DIDIER HAAS等;《Nuclear Technology》;19941231;第106卷(第1期);第60-82页 * |
| MOX燃料混料过程的优化;李怀林等;《原子能科学技术》;20010331;第35卷(第2期);第139-146页 * |
| 先进MOX燃料制造过程中创新的粉末生产和造粒方法;T.Kurita等;《国外核科技文献选编——核科技译丛十周年文集》;20141201;第407-413页 * |
| 快堆嬗变燃料(U-Np)O2芯块制备工艺研究;李强等;《中囯核科学技术进展报告(第四卷)核材料分卷》;20150930;第265-271页 * |
| 模拟MOX燃料粉末混合均匀性研究;尹邦跃等;《原子能科学技术》;20050731;第39卷;第125-130页 * |
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| CN107845433A (en) | 2018-03-27 |
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