DE1901784A1 - Dry reprocessing ceramic nuclear fuel - waste - Google Patents
Dry reprocessing ceramic nuclear fuel - wasteInfo
- Publication number
- DE1901784A1 DE1901784A1 DE19691901784 DE1901784A DE1901784A1 DE 1901784 A1 DE1901784 A1 DE 1901784A1 DE 19691901784 DE19691901784 DE 19691901784 DE 1901784 A DE1901784 A DE 1901784A DE 1901784 A1 DE1901784 A1 DE 1901784A1
- Authority
- DE
- Germany
- Prior art keywords
- nuclear fuel
- waste
- powder
- sieving
- dry reprocessing
- 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.)
- Pending
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)
- Combined Means For Separation Of Solids (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
Verfahren zur trockenen Aufarbeitung von keramischen UO2-Kernbrennstoff-Schrotten. Process for the dry processing of ceramic UO2 nuclear fuel scrap.
Zusatz zum Patent . (Anmeldung P 16 67 851.6) Bei der Durchführung des den Gegenstand des Hauptpatents bildenden Verfahrens hat sich gezeigt, dass die Vermischung der feinteiligen, zur Aggloseratbildung neigenden Schrottpulver mit dem U02-Ausgangspulver in beliebigen Mischapparaten zwar zu einer guten Makrohomogenität führt, die Mikrohomogenität der Misohung wegen der Bildung von grdsseren Agglomeraten ( >150 /u) beim Mischen der Komponenten in gewissen Fällen zu wünschen übrig lässt. Addition to the patent. (Registration P 16 67 851.6) During the implementation of the process forming the subject of the main patent has shown that the mixing of the finely divided scrap powder, which tends to form agglomerates with the U02 starting powder in any mixer to achieve good macro homogeneity leads to the microhomogeneity of the mixture due to the formation of larger agglomerates (> 150 / u) left to be desired in certain cases when mixing the components leaves.
Diese ungenügende Mikrohomogenität macht sich am geschliffenen Pellet durch das Auftreten grösserer Poren von einigen 100 Durchmesser bemerkbar. Diese Poren entstehen duroh das unterschiedliche Sinterverhalten von Sohrottpulveragglomeraten im umgebenden Ausgangspulver.This insufficient microhomogeneity is reflected in the ground pellet noticeable through the appearance of larger pores with a diameter of several hundred. These Pores are created by the different sintering behavior of soot powder agglomerates in the surrounding starting powder.
Poren der genannten Grösse im Sinterkörper werden nioht in jedem Fall toleriert, eo dass je nach Speziiikation die Ausschussquoten eine untragbare Höhe erreichen können.Pores of the size mentioned in the sintered body are not created in any case tolerated, eo that, depending on the speciiication, the reject rates can be unsustainable reachable.
Es wurde nun gefunden, dass die beschriebenen Nachteile sich dadurch vermeiden lassen, dass das erzeugte Urandioxidpulver einer Passiersiebung unterworfen wird. Dies PassIrsiebung erfolgt vorzugsweise in eine. Sieb iit einer Maschenweite von 63 µ bis 200 µ.It has now been found that the disadvantages described are thereby eliminated prevent the uranium dioxide powder produced from being subjected to sieving will. This passport screening is preferably carried out in a. Sieve with one mesh size from 63 µ to 200 µ.
Die Durchführung der Passiersiebung bringt darüber hinaus eine wesentliche Vereinfachung des vorhergehenden Verfahrensschrittes, da nunmehr beim Einbringen der Pulverkomponenten in einen apparativ einfachen Freifallmischer und beim ansohliessenden Mischen keine besondere Sorgialt mehr nötig ist.Carrying out the sieving process is also essential Simplification of the previous process step, since it is now being introduced the powder components in a simple free-fall mixer and with the attached Mixing is no longer necessary.
In der Abbildung ist eine Vorrichtung zur Durchführung der Passiersiebung dargestellt. Das ungesiebte Material wird hierbei über ein Zyklon 1 und eine Transportschnecke 2 der Siebvorrichtung 3 zugeführt, die aus einem zylindrischen Siebkorb mit innenliegendem rotierendem Schlägerwerk besteht. Das aus dem zylindrischen Siebkorb nach aussen austretende Pulver fällt über einen konischen Pulverauslaui 4 in eine Rohrleitung 5, aus der das gesiebte Material pneumatisch direkt in einen Vorratsbehälter gefördert wird.In the picture is a device for carrying out the sieving shown. The unscreened material is transported through a cyclone 1 and a screw conveyor 2 of the screening device 3 supplied, which consists of a cylindrical screen basket with an internal rotating racket. That out of the cylindrical strainer basket emerging powder falls through a conical powder outlet 4 into a pipeline 5, from which the screened material is pneumatically conveyed directly into a storage container will.
Beispiel: Die Herstellung der feinteiligen U02- bzw. U308-Pulver aus den verschiedenartigen Schrotten, die während der lXelletfertigung beim Pressen, Sintern und Schleifen anfallen und die Vermisohung dieser sogenannten Schrottpulver mit dem sinterfähigen U02-Ausgangspulver eriolgen wie in der hauptanmeldung P 16 67 851.6 in den Beispielen 1 bis 4 beschreiben.Example: The production of the finely divided U02 or U308 powder from the various types of scrap produced during pressing during lXellet production, Sintering and grinding occur and the misery of this so-called scrap powder with the sinterable U02 starting powder as in the main application P 16 67 851.6 in Examples 1 to 4.
Die erwünschte Mikrohomogenität (keine Agglonerste 100/u) dieser Pulvermischungen wurde duroh eine Passiersiebung bei 100 /u Maschenweite mit einem Hochleistungepassiersieb (Durohsatz: 19 to U02/n2U) erzielt. Die so erzeugten Pulvermischungen wurden pneumatisch direkt in den Pressenbunker gefördert und auf bekannte Weise zu UO2-Sinterkörpern verarbeitet. Ein Unterschied in Qualität und Ausbringung zwischen diesen Pulvermischungen und einem frischen sinterfähigen U0s-Pulver wurde nicht festgestellt.The desired microhomogeneity (no agglomerates 100 / u) of these powder mixtures was duroh a pass sieve at 100 / u mesh size with a high-performance pass sieve (Durohsatz: 19 to U02 / n2U) achieved. The powder mixtures thus produced became pneumatic conveyed directly into the press bunker and in a known way to UO2 sintered bodies processed. A difference in quality and output between these powder mixtures and a fresh sinterable U0s powder was not established.
Claims (4)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19691901784 DE1901784A1 (en) | 1969-01-15 | 1969-01-15 | Dry reprocessing ceramic nuclear fuel - waste |
SE1263/69A SE346048B (en) | 1968-02-01 | 1969-01-30 | |
FR6901932A FR2001113A1 (en) | 1968-02-01 | 1969-01-30 | PROCESS FOR THE DRY TREATMENT OF CERAMIC UO2 NUCLEAR FUEL SHOTS, AS WELL AS THE PRODUCTS OBTAINED |
BE727807D BE727807A (en) | 1968-02-01 | 1969-01-31 | |
ES369686A ES369686A1 (en) | 1969-01-15 | 1969-07-19 | Dry reprocessing ceramic nuclear fuel - waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19691901784 DE1901784A1 (en) | 1969-01-15 | 1969-01-15 | Dry reprocessing ceramic nuclear fuel - waste |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1901784A1 true DE1901784A1 (en) | 1970-09-17 |
Family
ID=5722453
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19691901784 Pending DE1901784A1 (en) | 1968-02-01 | 1969-01-15 | Dry reprocessing ceramic nuclear fuel - waste |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1901784A1 (en) |
ES (1) | ES369686A1 (en) |
-
1969
- 1969-01-15 DE DE19691901784 patent/DE1901784A1/en active Pending
- 1969-07-19 ES ES369686A patent/ES369686A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
ES369686A1 (en) | 1971-06-01 |
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