JPH0731267B2 - Manufacturing method of nuclear fuel pellets - Google Patents
Manufacturing method of nuclear fuel pelletsInfo
- Publication number
- JPH0731267B2 JPH0731267B2 JP1285536A JP28553689A JPH0731267B2 JP H0731267 B2 JPH0731267 B2 JP H0731267B2 JP 1285536 A JP1285536 A JP 1285536A JP 28553689 A JP28553689 A JP 28553689A JP H0731267 B2 JPH0731267 B2 JP H0731267B2
- Authority
- JP
- Japan
- Prior art keywords
- sio
- nuclear fuel
- powder
- producing
- added
- 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.)
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Classifications
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- 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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- Compositions Of Oxide Ceramics (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は原子力用セラミックスの製造方法、特に結晶粒
径が大きく、かつクリープ速度の大なる核燃料ペレット
の製造法に関するものである。TECHNICAL FIELD The present invention relates to a method for producing nuclear ceramics, and more particularly to a method for producing nuclear fuel pellets having a large crystal grain size and a high creep rate.
(従来の技術) 高燃焼度用UO2ペレットはFP(核分裂生成物)保持性が
良好なこと及びPCMI(ペレットと被覆管の機械的相互作
用)特性が良好なこと、即ちPCMIを軽減できることが求
められ、前者に対しては結晶粒径を大きくすること、、
後者に対しては軟らかいペレットとすることが試みられ
ている。(Prior Art) UO 2 pellets for high burnup have good FP (fission product) retention and good PCMI (mechanical interaction between pellet and cladding), that is, PCMI can be reduced. It is sought to increase the grain size of the former,
For the latter, attempts have been made to make soft pellets.
ところで従来、かかるペレットの製造に際し二酸化ウラ
ン(UO2)燃料へ種々の添加物を添加し上記の如きペレ
ット製造を目指すことが進められ、(1)特開昭55−27
941号公報,(2)特開昭55−27942号公報,(3)特公
昭54−8837号公報,(4)特公昭63−16716号公報,お
よび(5)特開昭63−73189号公報などにその幾つかが
開示されている。By the way, conventionally, in the production of such pellets, various additives have been added to uranium dioxide (UO 2 ) fuel to aim at the production of pellets as described above. (1) JP-A-55-27
941 gazette, (2) JP-A-55-27942, (3) JP-B-54-8837, (4) JP-B-63-16716, and (5) JP-A-63-73189. Some of them are disclosed in.
即ち、(1)特開昭55−27941号公報ではUO2に少なくと
も1種の容易に固溶せず、粒界に析出する特性のある添
加物を加えることが、また(2)特開昭55−27942号公
報ではUO2にAl2O3,BeO,CaO,MgO,SiO2,Na2O,P2O5から2
種以上を0.2〜5%添加することが、更に(3)特公昭5
4−8837号公報ではUO2に核分裂生成物不動化添加剤とし
てケイ酸アルミ,ケイ酸カルシウム,ケイ酸マグネシウ
ム,SiO2−Al2O3−MgO,SiO2−Al2O3−CaO,チタン酸アル
ミ,チタン酸ケイ素,CaO−SiO2−チタン酸塩等を加える
ことが夫々示されている。That is, (1) in JP-A-55-27941, at least one kind of additive that does not easily form a solid solution with UO 2 but precipitates at grain boundaries is added. In the 55-27942 publication, UO 2 is converted into Al 2 O 3 , BeO, CaO, MgO, SiO 2 , Na 2 O, P 2 O 5 to 2
Addition of 0.2 to 5% of seeds or more is (3) Japanese Patent Publication No. 5
In U.S. Pat. No. 4,88,37, aluminum silicate, calcium silicate, magnesium silicate, SiO 2 —Al 2 O 3 —MgO, SiO 2 —Al 2 O 3 —CaO, titanium are added to UO 2 as fission product immobilization additives. acid aluminum, silicon titanate, CaO-SiO 2 - be added titanates like are shown respectively.
また、(4)特公昭63−16716号公報ならびに(5)特
開昭63−73189号公報では上記UO2にAl2O3,BeO,CaO,MgO,
SiO2,Na2O,P2O5から2種以上の外、更にNb2O5,TiO2を添
加することが述べられている。Further, (4) JP-B 63-16716 discloses and (5) to the UO 2 in JP 63-73189 discloses Al 2 O 3, BeO, CaO , MgO,
It is stated that two or more kinds of SiO 2 , Na 2 O and P 2 O 5 are added, and Nb 2 O 5 and TiO 2 are further added.
(発明が解決しようとする課題) しかしながら、上記の如き添加物添加の方法においてNb
2O5,TiO2等を添加したものは粒径が大きく、かつPCMI特
性も良好となるが、Nb2O5,TiO2等の残存のため、粒径の
割りにFP保持性の改善はあまり望むことが出来ない難が
あり、また、中性子経済上、物性の変化上もよくなく、
更にSiO2,Al2O3等の粒界析出特性のあるものと上記Nb2O
5,TiO2等の粒径増大効果のある添加物を組み合わせる方
法は複雑で好ましくない。(Problems to be Solved by the Invention) However, in the method of adding additives as described above, Nb
The ones to which 2 O 5 , TiO 2 etc. are added have a large particle size and good PCMI characteristics, but due to the residual Nb 2 O 5 , TiO 2 etc., FP retention is not improved relative to the particle size. There are difficulties that I can not hope for, and it is not good in terms of neutron economy and changes in physical properties,
Furthermore SiO 2, Al 2 some of the grain boundary precipitation characteristics of O 3, and the Nb 2 O
5 , a method of combining additives such as TiO 2 having a particle size increasing effect is complicated and not preferable.
一方、ペレット製造に際し、高温長時間焼結を行うこと
は粒径は大きくなるが硬くなり、PCMI特性を低下させる
結果を招来する。On the other hand, in the production of pellets, performing high temperature and long time sintering increases the grain size but makes it harder, resulting in a decrease in PCMI characteristics.
なお二酸化ウラン燃料へAl2O3やSiO2を単味で添加して
特性の改良を試みた例も従来より数多くあるが、いずれ
も望ましい結果は得られておらず、結晶粒径の粗大化に
ついて言及しているものは殆ど見当たらない。It should be noted that there are many examples in which Al 2 O 3 or SiO 2 was simply added to the uranium dioxide fuel to improve the characteristics, but none of them have produced the desired results, and the crystal grain size was increased. There is almost nothing that mentions.
特に上記種々の添加物を入れる場合には通常、一部を除
いて0.1%以上の添加が必要であり、多くの場合、現
在、規定されている不純物量を越えている。上記Al2O3
及びSiO2の添加についても0.1wt%かつSiO2>Al2O3が限
度である。In particular, when the above-mentioned various additives are added, it is usually necessary to add 0.1% or more except for a part thereof, and in many cases, the amount of impurities currently specified is exceeded. Al 2 O 3 above
And 0.1 wt% also for the addition of SiO 2 and is SiO 2> Al 2 O 3 is the limit.
そこで、本発明者は上記の如き実状に対処し、その改善
を図るべく検討を重ね、その結果UO2に対するAl2O3とSi
O2の添加量を特定範囲に規定することを見出し、さらに
提案した。(特願平1−64868号)本発明は上記提案に
係る発明に更に一歩、進め、添加するAl2O3およびSiO2
の粉末の大きさと、その処理の仕方を加味することによ
り結晶粒径を大ならしめると共にやわらかいペレットの
製造を可能にし、FP保持性ならびにPCMI特性をより一層
向上せしめることを目的とするものである。Therefore, the present inventor has dealt with the actual situation as described above, and has conducted repeated studies to improve it. As a result, Al 2 O 3 and Si with respect to UO 2
The inventors have found that the amount of O 2 added is limited to a specific range, and further proposed it. (Japanese Patent Application No. 1-64868) The present invention goes one step further than the invention of the above-mentioned proposal, and adds Al 2 O 3 and SiO 2
The purpose of the present invention is to increase the crystal grain size and enable the production of soft pellets by taking into consideration the size of the powder and the treatment method, and further improve the FP retention and PCMI characteristics. .
(課題を解決するための手段) 即ち、上記目的を適合する本発明の特徴は、ウラン,プ
ルトニウムの少なくとも1つの元素の二酸化物または前
記物質にガドリニアを添加した核燃料物質にAl2O3およ
びSiO2を添加し核燃料ペレットを製造するにあたり、前
記Al2O3およびSiO2の粉末を特に粒度1μm以下の超微
粉末とし、その添加量を0.005%〜0.05%,かつAl2O3と
SiO2の重量比を1:1〜30:1の範囲としてそれらを混合し
た粉末を成型することであり、かつその後、水素を含む
還元雰囲気で本体雰囲気ガス流量に対して40〜70℃の飽
和水蒸気を含むキヤリヤーガスを体積率で0.1〜10%添
加し、1600〜1750℃で2〜6時間焼結することにある。(Means for Solving the Problems) That is, the feature of the present invention which meets the above object is that Al 2 O 3 and SiO are added to a dioxide of at least one element of uranium and plutonium or a nuclear fuel substance obtained by adding gadolinia to the substance. When adding 2 to produce a nuclear fuel pellet, the powder of Al 2 O 3 and SiO 2 is made into an ultrafine powder with a particle size of 1 μm or less, and its addition amount is 0.005% to 0.05% and Al 2 O 3 .
The weight ratio of SiO 2 is in the range of 1: 1 to 30: 1, and the powders are mixed to form a powder, and thereafter, in a reducing atmosphere containing hydrogen, saturation of 40 to 70 ° C with respect to the main body gas flow rate is performed. This is to add a carrier gas containing water vapor in an amount of 0.1 to 10% by volume and sinter at 1600 to 1750 ° C. for 2 to 6 hours.
ここで成型後の雰囲気は上記の場合、水素を含む還元雰
囲気であるが、酸素濃度100ppm以下の微酸化雰囲気下例
えば酸素を微量含むCO2雰囲気下又はCO2/CO雰囲気下で
あっても差し支えなく、請求項2記載の方法はかかる場
合である。Here, the atmosphere after molding is a reducing atmosphere containing hydrogen in the above case, but it may be a slightly oxidizing atmosphere having an oxygen concentration of 100 ppm or less, for example, a CO 2 atmosphere containing a small amount of oxygen or a CO 2 / CO atmosphere. However, the method according to claim 2 is such a case.
また、請求3記載の発明は上記各方法におけるAl2O3お
よびSiO2の添加の態様に係り、ケイ酸アルミニウム又は
ケイ酸アルミニウムにAl2O3を添加することによって行
うこと、請求項4記載の発明は更にその場合においてケ
イ酸アルミニウム粉末として1μm以下の超微粉末を用
いることを特徴とする。The invention according to claim 3 relates to the mode of adding Al 2 O 3 and SiO 2 in each of the above methods, and is carried out by adding Al 2 O 3 to aluminum silicate or aluminum silicate. The invention of 1) is further characterized in that in that case, ultrafine powder of 1 μm or less is used as the aluminum silicate powder.
請求項5及び6に記載した方法は更に前記発明を実施す
るに際し、適用される好ましい態様に係り、前者はAl2O
3,SiO2またケイ酸アルミニウムの混合時、カッターミル
やボールミル混合のように粉末の粉砕を含む混合を行う
ことであり、後者は粒径に影響なく密度の調整および成
型を容易にするためにPVA等の造粒剤,ステアリン酸等
の潤滑材,澱粉,U3O8,パルチミン酸等のポア形成剤を添
加することを特徴とする。The method described in claims 5 and 6 relates to a preferred embodiment applied when carrying out the invention, wherein the former is Al 2 O.
When mixing 3 , SiO 2 and aluminum silicate, it is necessary to perform mixing including pulverization of powder such as mixing with a cutter mill or a ball mill. The latter is for facilitating density adjustment and molding without affecting particle size. It is characterized by adding a granulating agent such as PVA, a lubricant such as stearic acid, and a pore-forming agent such as starch, U 3 O 8 and palmitic acid.
(作用) 上記の方法により核燃料ペレットを製造するときは種々
の添加物を添加することなく、簡単な方法であるにかか
わらず、現在のUO2ペレットのスペックである。(Operation) When manufacturing nuclear fuel pellets by the above-mentioned method, it is a specification of the present UO 2 pellets, though it is a simple method without adding various additives.
Al含有率 100ppm以下、 Si含有率 250ppm以下、 を十分満足し、かつ、粒径が通常方法による〜10μmに
対し、インターセプト法による平均結晶粒径が30〜60μ
mの大粒径ペレットで、かつクリープ速度が粒径補正を
しなくても、5×102〜103倍程度の大きなペレットを得
ることを可能ならしめる。The Al content is 100ppm or less and the Si content is 250ppm or less, and the average grain size by the intercept method is 30-60μ, while the grain size by the usual method is ~ 10μm.
This makes it possible to obtain pellets having a large particle size of m and having a creep rate of about 5 × 10 2 to 10 3 times as large as that without correcting the particle size.
以下、本発明の具体的な実施例につき説明する。Hereinafter, specific examples of the present invention will be described.
(実施例1) Al2O3中のAlの含有率53%、SiO2中のSi含有率47%で、
これよりUO2のAl,Siの規格を夫々Al100ppm,Si250ppmと
すると、Al2O3の最大添加量は0.02%、SiO2の最大添加
量は0.05%である。(Example 1) With an Al content of 53% in Al 2 O 3 and a Si content of 47% in SiO 2 ,
From this, when the specifications of Al and Si of UO 2 are Al 100 ppm and Si 250 ppm, the maximum addition amount of Al 2 O 3 is 0.02% and the maximum addition amount of SiO 2 is 0.05%.
このため、UO2粉末へのAl2O3とSiO2の添加総量を0.01%
として下記の如き混合率、焼結条件の下に各実験を行っ
た。Therefore, the total amount of Al 2 O 3 and SiO 2 added to UO 2 powder should be 0.01%.
Each experiment was conducted under the following mixing ratio and sintering conditions.
(イ)混合率 (ロ)焼結条件 1750℃×4Hr,H2/N2雰囲気であるが、水(水蒸気)添加
量をキヤリヤーガス比で、ケース(1)は0.1%、ケー
ス(2)は10%とした。(A) Mixing rate (B) Sintering conditions 1750 ° C. × 4 Hr, H 2 / N 2 atmosphere, but the amount of water (steam) added was 0.1% for case (1) and 10% for case (2) in terms of carrier gas ratio.
これは40〜70℃の温湯から出る水蒸気にアルゴンキヤリ
ヤーガスを通して、これを含ませたものを、本体雰囲気
ガスに合流させるが、このときの合流させる体積率が0.
1〜10%になるようにアルゴンガス流量をセットして行
った。This is the steam that comes out of the hot water of 40-70 ℃, let the argon carrier gas pass through it, and let the gas that contains it join the main body atmosphere gas, but the volume ratio at this time is 0.
Argon gas flow rate was set so that it was 1 to 10%.
なお、上記実験においてキヤリヤーガスとしてはアルゴ
ンガスを用いたが、勿論、これはN2又はN2/H2であって
も差し支えない。In the above experiment, argon gas was used as the carrier gas, but of course, this may be N 2 or N 2 / H 2 .
上記による実験の結果、インターセプト法による粒径の
変化は下記の通りであった。As a result of the above experiment, the change in particle size by the intercept method was as follows.
上表によるケース(1)のCの場合における結晶粒径を
顕微鏡観察により観察した結果を第1図に、またUO2の
みのケース(1)のDの場合における結晶粒径の顕微鏡
観察結果を第3図に夫々示す。これら両図を観察するこ
とにより第1図では第3図の粒径に比して大粒径化して
いることを知見される。 Fig. 1 shows the results of observing the crystal grain size in the case of C in case (1) according to the table above, and Fig. 1 shows the results of the crystal grain size in the case of case (1) in the case of UO 2 only. Each is shown in FIG. By observing both of these figures, it is found that the particle size in FIG. 1 is larger than that in FIG.
また、上記ケース(1)のCの混合粉末にポア形成剤と
してパルチミン酸を0.1%加え、同様に実験を試みたと
ころ、パルチミン酸混入による粒径への影響は全く認め
られなかった。(第3図参照) (実施例2) UO2粉末にガドリア(Gd2O3)を8%添加して、これを原
料として上記実施例1と同様に実験を行ったところAl2O
3/SiO2無添加の場合の平均粒径が1〜3μm(第5図参
照)であったのに対し、Al2O3/SiO2の混合比が5の粉末
をAl2O3とSiO2の添加総量において0.01%で加えた混合
粉末を前記同様、1750℃×4Hr,H2/N2雰囲気で焼結した
ものは粒径が大きく10〜20μm(第4図参照)へ増加す
ることが認められた。Further, when 0.1% of palmitic acid as a pore-forming agent was added to the mixed powder of C in the above case (1) and the same experiment was attempted, no influence on the particle size due to the incorporation of palmitic acid was observed. (See FIG. 3) (Example 2) UO 2 powder Gadoria (Gd 2 O 3) and was added 8%, Al 2 O where it was subjected to the same experiment as in Example 1 as a starting material
Whereas the average particle size was 3 μm (see Fig. 5) when 3 / SiO 2 was not added, powders with a mixing ratio of Al 2 O 3 / SiO 2 of 5 were mixed with Al 2 O 3 and SiO 2. As in the above case, the mixed powder added at 0.01% in the total addition amount of 2 was sintered in the 1750 ° C. × 4Hr, H 2 / N 2 atmosphere, and the particle size increased to 10 to 20 μm (see FIG. 4). Was recognized.
また同様にして実施例1の混合率で夫々実験を試みたと
ころ、何れもその添加により10〜20μmへ粒径が増加す
ることが確認された。Further, similar experiments were conducted at the mixing ratios of Example 1, respectively, and it was confirmed that the addition of any of them increased the particle size to 10 to 20 μm.
この場合、水蒸気添加による水添加の効果は明確とは云
えないが、微小粒の減少となって現れていた。In this case, the effect of water addition by adding steam was not clear, but it appeared as a reduction of fine particles.
なお、PVA(ポリビニルアルコール)等の造粒剤、ステ
アリン酸等の潤滑剤、澱粉、U3O8、パルミチン酸等のポ
ア形成剤を適宜、用いたが、これらは粒径への影響なく
使用可能であった。Granular agents such as PVA (polyvinyl alcohol), lubricants such as stearic acid, and pore-forming agents such as starch, U 3 O 8 and palmitic acid were used as appropriate, but these can be used without affecting the particle size. It was possible.
また、上記実施例で得られた焼結体を試料として1400
℃,45MPaの高温クリープ試験を実施したところ、何れの
場合も粒径補正を行なわなくて無添加UO2に比して5×1
02〜103倍のクリープ速度を有しており、頗るすぐれた
セラミック燃料であった。In addition, the sintered body obtained in the above example was used as a sample for 1400
° C., was subjected to a high-temperature creep test of 45 MPa, as compared with additive-free UO 2 without performing the particle diameter compensation either case 5 × 1
It had a creep rate of 0 2 to 10 3 times and was an excellent ceramic fuel.
(発明の効果) 本発明は以上のように核燃料物質にAl2O3およびSiO2を
添加し核燃料ペレットを製造するに際しAl2O3およびSiO
2の粉末粒度を1μm以下とし、その添加総量を0.005%
〜0.05%、かつAl2O3とSiO2の重量比を1:1〜30:1の範囲
として成型し、焼結する方法であり、上記の如くAl2O3
とSiO2の粉末粒度および量を規定することにより不純物
スペックの範囲内のAl2O3とSiO2を添加するだけで、よ
り簡単により少量の添加物で高燃焼度UO2ペレットに要
求されるような従来製法によるUO2ペレットの結晶粒径
の3〜10倍の結晶粒径をもつ大粒径かつ大クリープ速度
のセラミック燃料を得ることが可能となり、FP保持性な
らびにPCMI特性の改善に顕著な効果を奏し、今後に関心
がもたれるような上記高燃焼度用UO2ペレットの工業的
かつ経済的製造分野にその適用が期待されるものであ
る。Al 2 O 3 and SiO upon (Effect of the Invention) The present invention is the production of nuclear fuel pellets by adding Al 2 O 3 and SiO 2 in the nuclear fuel material as above
The powder particle size of 2 is 1 μm or less, and the total addition amount is 0.005%
0.05%, and Al 2 O 3 and the weight ratio of SiO 2 1: 1 to 30: molding a first range, a method of sintering, Al 2 O 3 as described above
By simply adding Al 2 O 3 and SiO 2 within the impurity specification range by defining the powder particle size and amount of SiO 2 and SiO 2 , it is possible to easily obtain high burnup UO 2 pellets with a smaller amount of additives. It is possible to obtain a ceramic fuel with a large grain size and a high creep rate, which has a grain size 3 to 10 times the grain size of UO 2 pellets by the conventional manufacturing method as described above, and it is remarkably improved in FP retention and PCMI characteristics. It is expected to be applied to the industrial and economical production field of the above-mentioned high burnup UO 2 pellets, which has various effects and is of interest in the future.
第1図は二酸化ウランにAl2O3/SiO2=5の混合比の粉末
を0.01%添加した実施例1のケース(1)Cで得られた
核燃料焼結体の結晶粒径金属顕微鏡観察にて400倍の倍
率で撮影した金属組織顕微鏡写真、第2図は上記第1図
の試料にポア形成剤としてパルチミン酸を0.1加えて得
られた核燃料焼結体の結晶粒径を金属顕微鏡で400倍の
倍率で撮影した金属組織顕微鏡写真、第3図は従来の二
酸化ウランのみで得られた実施例1のケース(1)Dに
よる核燃料焼結体の結晶粒体を金属顕微鏡で400倍の倍
率で撮影した金属組織顕微鏡写真、第4図は二酸化ウラ
ンにガドリニアを8%添加したガドリニア入りUO2粉末
に更にAl2O3/SiO2=5の混合粉末を0.01%加え焼結した
ペレットの結晶粒径を前記同様、金属顕微鏡観察で400
倍の倍率で撮影した金属組織顕微鏡写真、第5図は上記
第4図におけるガドリア8%添加UO2ペレットの結晶粒
径を金属顕微鏡観察で400倍の倍率で撮影した金属組織
顕微鏡写真である。FIG. 1 shows a crystal grain size metallographic observation of a nuclear fuel sintered body obtained in case (1) C of Example 1 in which 0.01% of powder having a mixing ratio of Al 2 O 3 / SiO 2 = 5 was added to uranium dioxide. Micrograph of metallographic structure taken at 400x magnification in Fig. 2, Fig. 2 shows the crystal grain size of the nuclear fuel sintered body obtained by adding 0.1 parts of palmitic acid as a pore-forming agent to the sample in Fig. 1 with a metallographic microscope. A metallographic micrograph taken at a magnification of 400 times, and FIG. 3 shows a crystal grain of a nuclear fuel sintered body according to Case (1) D of Example 1 obtained only with conventional uranium dioxide at a magnification of 400 times. A metallographic micrograph taken at a magnification, Fig. 4 shows a pellet of UO 2 powder containing 8% gadolinia added to uranium dioxide and 0.01% mixed powder of Al 2 O 3 / SiO 2 = 5 and sintered. The crystal grain size was 400 as observed with a metallographic microscope as above.
A metallographic micrograph taken at a magnification of 2 ×, and FIG. 5 is a metallographic micrograph taken at a magnification of 400 × of the crystal grain size of the UO 2 pellets containing 8% of Gadria shown in FIG.
Claims (6)
元素の二酸化物または前記物質にガドリニアを添加した
核燃料物質にAl2O3およびSiO2を添加し核燃料ペレット
を製造するにあたり、前記Al2O3およびSiO2の粉末を粒
度1μm以下の超微粉末とし、その添加総量を0.005%
〜0.05%、かつAl2O3とSiO2の重量比を1:1〜30:1の範囲
としてそれらを混合した粉末を成型し、のち、水素を含
む還元雰囲気で本体雰囲気ガス流量に対して40〜70℃の
飽和水蒸気を含むキヤリヤーガスを体積率で0.1〜10%
添加し、1600〜1750℃で2〜6時間焼結を行うことを特
徴とする核燃料ペレットの製造法。1. A method for producing a nuclear fuel pellet by adding Al 2 O 3 and SiO 2 to a nuclear fuel material obtained by adding gadolinia to a dioxide of at least one element of uranium and plutonium, or the above-mentioned Al 2 O 3 and The SiO 2 powder is made into an ultrafine powder with a particle size of 1 μm or less, and the total addition amount is 0.005%.
~ 0.05%, and the weight ratio of Al 2 O 3 and SiO 2 is in the range of 1: 1 to 30: 1 to form a mixed powder, and then in a reducing atmosphere containing hydrogen against the main body gas flow rate. Carrier gas containing saturated steam at 40-70 ℃ is 0.1-10% by volume.
A method for producing nuclear fuel pellets, which comprises adding and sintering at 1600-1750 ° C. for 2-6 hours.
元素の二酸化物または前記物質にガドリニアを添加した
核燃料物質にAl2O3およびSiO2を添加し核燃料ペレット
を製造するに際し、前記Al2O3およびSiO2の粉末を粒度
1μm以下の超微粉末とし、その添加総量を0.005%〜
0.05%、かつAl2O3とSiO2の重量比を1:1〜30:1の範囲と
してそれらを混合した粉末を成型し、成型後、酸素濃度
102ppm以下の微酸化雰囲気にて1600〜1750℃で2〜6時
間焼結を行うことを特徴とする核燃料ペレットの製造
法。2. In producing a nuclear fuel pellet by adding Al 2 O 3 and SiO 2 to a nuclear fuel material obtained by adding gadolinia to a dioxide of at least one element of uranium and plutonium, or the above-mentioned Al 2 O 3 and The SiO 2 powder is made into an ultrafine powder with a particle size of 1 μm or less, and the total addition amount is 0.005% to
0.05% and Al 2 O 3 and SiO 2 weight ratio in the range of 1: 1 to 30: 1 were mixed and molded into a powder, and the oxygen concentration after molding
A method for producing a nuclear fuel pellet, which comprises sintering at 1600 to 1750 ° C for 2 to 6 hours in a slightly oxidizing atmosphere of 10 2 ppm or less.
またはケイ酸アルミニウムにAl2O3を添加する方法で行
うことを特徴とする請求項1または2記載の核燃料ペレ
ットの製造法。3. The method for producing nuclear fuel pellets according to claim 1, wherein Al 2 O 3 and SiO 2 are added by aluminum silicate or a method of adding Al 2 O 3 to aluminum silicate. .
1μm以下の超微粉末とすることを特徴とする請求項3
記載の核燃料ペレットの製造法。4. An ultrafine powder having a powder particle size of aluminum silicate to be added of 1 μm or less.
A method for producing a nuclear fuel pellet as described.
加した後、カッターミル又はボールミルを用いて粉砕混
合を行うことを特徴とする請求項1,2,3又は4記載の核
燃料ペレットの製造法。5. The nuclear fuel pellet according to claim 1, 2, 3 or 4, wherein Al 2 O 3 , SiO 2 or aluminum silicate is added and then pulverized and mixed using a cutter mill or a ball mill. Manufacturing method.
度の調整および成型を容易にするためにPVA等の造粒
剤,ステアリン酸等の潤滑剤,澱粉,U3O8などのポア形
成剤をさらに添加することを特徴とする核燃料ペレット
の製造法。6. The manufacturing method according to claim 1, wherein granules such as PVA, lubricants such as stearic acid, starch, pores such as U 3 O 8 are included in order to facilitate density adjustment and molding. A method for producing a nuclear fuel pellet, which further comprises adding a forming agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1285536A JPH0731267B2 (en) | 1989-10-31 | 1989-10-31 | Manufacturing method of nuclear fuel pellets |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1285536A JPH0731267B2 (en) | 1989-10-31 | 1989-10-31 | Manufacturing method of nuclear fuel pellets |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03146895A JPH03146895A (en) | 1991-06-21 |
| JPH0731267B2 true JPH0731267B2 (en) | 1995-04-10 |
Family
ID=17692807
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1285536A Expired - Lifetime JPH0731267B2 (en) | 1989-10-31 | 1989-10-31 | Manufacturing method of nuclear fuel pellets |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0731267B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3843108A4 (en) * | 2019-09-25 | 2022-06-01 | Kepco Nuclear Fuel Co., Ltd. | NUCLEAR FUEL URANIUM DIOXIDE PELLETS HAVING IMPROVED FISSION GAS CAPACITY AND METHOD FOR MAKING THEM |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2603382B2 (en) * | 1991-03-04 | 1997-04-23 | 日本核燃料開発株式会社 | Nuclear fuel pellet and method for producing the same |
| JP2672420B2 (en) * | 1991-09-20 | 1997-11-05 | 日本核燃料開発株式会社 | Mixed oxide fuel pellet and method for producing the same |
| US5828715A (en) * | 1995-08-22 | 1998-10-27 | Hitachi, Ltd. | Fuel rods, its manufacturing method and fuel assembly |
-
1989
- 1989-10-31 JP JP1285536A patent/JPH0731267B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3843108A4 (en) * | 2019-09-25 | 2022-06-01 | Kepco Nuclear Fuel Co., Ltd. | NUCLEAR FUEL URANIUM DIOXIDE PELLETS HAVING IMPROVED FISSION GAS CAPACITY AND METHOD FOR MAKING THEM |
| US11742097B2 (en) | 2019-09-25 | 2023-08-29 | Kepco Nuclear Fuel Co., Ltd. | Uranium-dioxide pellet for nuclear fuel having improved nuclear-fission-gas adsorption property, and method of manufacturing same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03146895A (en) | 1991-06-21 |
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