DE1901784A1 - Dry reprocessing ceramic nuclear fuel - waste - Google Patents

Dry reprocessing ceramic nuclear fuel - waste

Info

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
Application number
DE19691901784
Other languages
German (de)
Inventor
Uwe Goeldner
Dipl-Ing Hans Pirk
Horst Dipl-Ing Roepenack
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nukem GmbH
Original Assignee
Nukem GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nukem GmbH filed Critical Nukem GmbH
Priority to DE19691901784 priority Critical patent/DE1901784A1/en
Priority to SE1263/69A priority patent/SE346048B/xx
Priority to FR6901932A priority patent/FR2001113A1/en
Priority to BE727807D priority patent/BE727807A/xx
Priority to ES369686A priority patent/ES369686A1/en
Publication of DE1901784A1 publication Critical patent/DE1901784A1/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21CNUCLEAR REACTORS
    • G21C3/00Reactor fuel elements and their assemblies; Selection of substances for use as reactor fuel elements
    • G21C3/42Selection of substances for use as reactor fuel
    • G21C3/58Solid reactor fuel Pellets made of fissile material
    • G21C3/62Ceramic fuel
    • G21C3/623Oxide fuels
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear 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

Dry reprocessing ceramic UO2 nuclear fuel waste To improve the microhomogeneity of the sintered dioxide power, as in 1667851, it is passed through a cylindrical screen with a rotating hammer mill inside. The mesh size of the screen may be 63 to 200 mu m but preferably 100 mu m.

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)

PATENTANSPRÜCHEPATENT CLAIMS 1. Verfahren zur trookenen Aufarbeitung von keramischen U02-Kernbrennstoff-Schrotten gemäss Patent ........1. Process for the dry reprocessing of ceramic U02 nuclear fuel scrap according to patent ........ (Anmeldung P 16 67 851.6), dadurch gekennzeichnet, dass das erzeugte Urandioxidpulver einer Passiersiebung unterworfen wird. (Registration P 16 67 851.6), characterized in that the generated Uranium dioxide powder is subjected to sieving. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Passiersiebung bei einer Maschenweite de.s Siebes von 63 /u bis 200 /u, ' vorzugsweise jedoch bei 100 erzielt wird.2. The method according to claim 1, characterized in that the pass sieving with a mesh size of the sieve from 63 / u to 200 / u, but preferably at 100 is achieved. 3. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Passiersiebung mit einem Passiersieb, bestehend aus einem zylindrischen Siebkorb mit innenliagendem rotierendem Schlägerwerk durchgeführt wird.3. The method according to claim 1, characterized in that the pass sieving with a strainer consisting of a cylindrical strainer basket with an inside rotating racket is carried out. 4. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Passiersiebung kontinuierlioh durchgeführt wird.4. The method according to claim 1, characterized in that the pass sieving is carried out continuously.
DE19691901784 1968-02-01 1969-01-15 Dry reprocessing ceramic nuclear fuel - waste Pending DE1901784A1 (en)

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)

Also Published As

Publication number Publication date
ES369686A1 (en) 1971-06-01

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