EP0081084A1 - Moulded body for encapsulating radioactive wastes, and process for manufacturing this body - Google Patents
Moulded body for encapsulating radioactive wastes, and process for manufacturing this body Download PDFInfo
- Publication number
- EP0081084A1 EP0081084A1 EP82110144A EP82110144A EP0081084A1 EP 0081084 A1 EP0081084 A1 EP 0081084A1 EP 82110144 A EP82110144 A EP 82110144A EP 82110144 A EP82110144 A EP 82110144A EP 0081084 A1 EP0081084 A1 EP 0081084A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- waste
- shell
- shaped body
- graphite
- pressed
- 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.)
- Withdrawn
Links
Images
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/28—Treating solids
- G21F9/30—Processing
- G21F9/301—Processing by fixation in stable solid media
- G21F9/302—Processing by fixation in stable solid media in an inorganic matrix
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/28—Treating solids
- G21F9/34—Disposal of solid waste
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/23—Sheet including cover or casing
- Y10T428/239—Complete cover or casing
Definitions
- Shaped body for the integration of radioactive waste and process for its production
- the invention relates to a shaped body made of graphite and an inorganic binder for the safe long-term incorporation of toxic. and radioactive waste, and a process for its production.
- a suitable, in particular corrosion and leach-resistant, binding matrix or a corresponding container material must ensure that the highly active waste that is stored remains at the storage location for a thousand years or more and does not return to the biosphere.
- radioactive waste generated during the reprocessing of spent fuel elements must be brought into a form suitable for disposal.
- a high level of waste is economically necessary. This requires a substantial volume reduction - for example by evaporation - before the solidification step.
- the waste is first calcined in a fluidized bed between 350 and 900 ° C.
- a mixture of oxides is obtained which is incorporated as a powder or granulate in a glass-like or ceramic matrix and thereby solidified to form a product that can be disposed of.
- Methods are known for embedding medium and low-level waste, according to which the waste materials e.g. heated with bitumen and subjected to an extrusion process.
- the radioactive waste is incorporated into the bitumen mass, hot filled into barrels and finally stored.
- Another method is to fix the radioactive waste in cement or concrete.
- the slurry is mixed with cement and allowed to set. If necessary, this step can be carried out directly in the final storage casks.
- Bituminization is only applicable to relatively low activity concentrations, e.g. for the so-called liquid medium-active waste of approx. 0.1 - 1 Ci ⁇ , ⁇ activity. Temperatures of 150 - 200 ° C are necessary, which requires complex safety precautions, e.g. against fire, required. In addition, under radiation, bitumen forms radiolysis gases, e.g. Hydrogen.
- the simple technique of cementing also has disadvantages. So you get large volumes of waste with the same amount of waste, e.g. 3 to 5 times the volume compared to bitumen inclusion, a relatively poor leaching behavior of the enclosed radioactive waste due to the porosity of the cement, and a radiolysis of the water bound in the cement, which can lead to relatively large amounts of gas, such as hydrogen.
- final storage containers which absorb the waste materials and are usually designed as multi-layer containers to achieve sufficient long-term corrosion resistance.
- Corrosion-resistant metallic and non-metallic materials are used as container materials.
- DE-OS 29 17 437 describes a process for incorporating radioactive and toxic waste into a good heat-conducting carbon matrix under mild conditions bind, which consists of a mixture of powdered carbon, preferably graphite, with a binder, wherein a corresponding shaped body is formed by pressing with the admixed waste at temperatures above 100 ° C.
- bind which consists of a mixture of powdered carbon, preferably graphite, with a binder, wherein a corresponding shaped body is formed by pressing with the admixed waste at temperatures above 100 ° C.
- Suitable binders are organic and inorganic substances, the use of sulfur is advantageous and in a preferred embodiment a mixture of sulfur and nickel is used which forms the water-insoluble nickel sulfide at a pressing temperature of about 400 ° C.
- this matrix is resistant to corrosion and leaching, the waste materials can be removed from the surface layer in the case of the molded articles produced by adding the waste to the matrix starting materials.
- the highest possible concentration of waste is in the. Moldings required. In the case of higher proportions of waste in the molded article, the waste is leached out in the long term from ever deeper layers and ultimately from the entire molded article.
- the molded body consists of a core in which the waste is embedded and a waste-free shell made of the same material.
- the graphite matrix for core and shell is produced in a known manner by pressing a mixture of powdered graphite and an inorganic binder or the starting components of an inorganic binder at a temperature above 100 ° C. Either sulfur or a stable metal sulfide is used as the inorganic binder. It is advantageous to use an easily compressible natural graphite powder as graphite.
- a pressing temperature in the range of the melting temperature of the sulfur of approximately 120 ° C. and a pressing pressure of 10-50 MN / m 2 , preferably approximately 20 MN / m 2 are used.
- a core and shell shaped body produced in this way is suitable for toxic and low-level radioactive waste which only generates a small amount of heat. Greater decay heat occurs in more radioactive waste, particularly in the case of highly active waste, which requires high thermal stability of the graphite matrix.
- nickel for example, lead, iron, nickel, cobalt, copper, molybdenum, vanadium or tungsten can be used as metals.
- the use of nickel to form nickel sulfide has proven to be particularly advantageous.
- the proportion of waste in the core is advantageously between 1 and 70% by volume, preferably between 10 and 50% by volume, so that the core is in the form of a mechanically stable body which has essentially the same physical properties as the waste-free shell.
- a pressing temperature of 130 ° C and a pressing pressure of about 20 to 50 MN / m 2 are sufficient to produce a high-density, corrosion and leach-resistant molded body.
- the connection between the inner zone and the shell is preferably carried out at a temperature above 300 ° C. and a pressure of 30 to 100 MN / m 2 .
- the core is preferably also initially pressed at room temperature or at elevated temperature and the compact is inserted into a pre-pressed hollow cylinder with an attached base. After placing the cover plate, the entire molded body is pressed at a temperature above 100 ° C and compressed to over 80% of the theoretical density. With continued pressure, the temperature is raised to above 400 ° C, preferably to about 440 ° C.
- the molded body which is ejected after cooling to below 400 ° C., has a density above 90% of the theoretical value and is highly dense and free of continuous pores.
- the shaped body according to the invention is chemically extremely stable, i.e. still very corrosion and leach resistant even in highly corrosive media.
- the waste-containing core in the interior of the waste-free shell has largely the same physico-chemical characteristics as the casing, so that mechanical stresses that can cause the container to tear are practically eliminated.
- the core (1) of the cylindrical shaped body consists of a matrix of graphite with an inorganic binder, in which the granular or lumpy radioactive waste (2) is embedded.
- the core (1) is surrounded on all sides by the waste-free shell (3), with which it is connected without transition.
- the places where the shell (3) is assembled from preformed annular sections (4) are shown in dashed lines.
- the shell (3) is surrounded by a steel shell (5).
- a compact made of the same matrix and containing 50 vol.% Waste is inserted into this container-like cavity.
- the cover plate is then placed on and connected to the hollow cylinder to form a closed shell under the same conditions as specified for the segments.
- the pulverulent mixture prepared in the same way as in Example 1 from the starting components of the graphite matrix is mixed with approximately the same amount of feed sludge simulate, which consists of molybdenum, molybdenum (VI) oxide, manganese, manganese ( IV) oxide, zirconium, calcium chloride, antimony (III) oxide, stainless steel and nickel powder.
- feed sludge simulate which consists of molybdenum, molybdenum (VI) oxide, manganese, manganese ( IV) oxide, zirconium, calcium chloride, antimony (III) oxide, stainless steel and nickel powder.
- This mixture is transferred to the hollow cylinder made of graphite-nickel-sulfur matrix, which is pre-pressed at room temperature and is located in a die that can be heated from the outside.
- the entire molded body in the melting range of the sulfur - at 130 ° C - is compressed with a pressure of about 100 MN / m 2 , the temperature is increased to 450 ° C at constant pressure and the sulfur is converted to nickel sulfide . After cooling to about 350 ° C., the molded article containing the simulate is ejected. In addition to the physical properties mentioned in Example 1, particularly low Cs leaching rates are observed on this body: 3. 10 -4 - 5 x 10 -6 c m / d.
- the powdery matrix components graphite, sulfur and nickel are first mixed intensively in accordance with Example 1.
- About 3 cm long sections of fuel rod sleeves (sleeve diameter outside 10.75 mm; wall thickness 0.68 mm) made of Zirkaloy-4 are mixed into the press powder formed.
- the proportion by weight of the compacted or uncompacted sleeves is 25% by weight.
- the sleeve / pressed powder mixture is pre-pressed at room temperature in a floating steel die (inner diameter 50 mm) with a pressure of about 5 MN / m 2 .
- the "core" formed (diameter 50 mm, height 80 mm) has about 50% of the theoretical density.
- the pre-pressed "core” is then inserted in a heatable press mold into the parts of the shell which have also been pre-shaped at room temperature and with a pressure of 5 MN / m 2 ; the shell consists of a base plate, a hollow cylinder with an outer diameter of 66 mm and a cover plate.
- the molded body is compressed with a pressure of 50 MN / m 2 to about 85% of the theoretical density.
- the almost finished test specimen is heated to a temperature of around 440 ° C under constant pressure.
- the nickel / sulfur mixture converts into the chemically, mechanically and thermally much more stable nickel sulfide. At the same time, the density increases to over 90% of the theoretical value.
- the finished test specimen is cooled to 350-400 ° C. and ejected (diameter 66 mm, height approximately 75 mm).
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Carbon And Carbon Compounds (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
Zur sicheren Langzeit-Einbindung von radioaktiven und toxischen Abfällen sind Formkörper bekannt, die eine Matrix aus Graphit und einem anorganischen Bindemittei, vorzugsweise Nickelsulfid, besitzen. Eine erhöhte Auslaugbeständigkeit erreicht man mit Formkörpern, die einen abfallhaltigen Kern und eine abfallfreie Schale aus der gleichen Graphitmatrix besitzen.Shaped bodies are known for the safe long-term integration of radioactive and toxic waste, which have a matrix of graphite and an inorganic binder, preferably nickel sulfide. Increased leaching resistance is achieved with moldings that have a waste-containing core and a waste-free shell made from the same graphite matrix.
Description
Formkörper zur Einbindung radioaktiver Abfälle und Verfahren zu seiner HerstellungShaped body for the integration of radioactive waste and process for its production
Die Erfindung betrifft einen Formkörper aus Graphit und einem anorganischen Bindemittel zur sicheren Langzeit-Einbindung von toxischen. und radioaktiven Abfällen, und ein Verfahren zu-seiner Herstellung.The invention relates to a shaped body made of graphite and an inorganic binder for the safe long-term incorporation of toxic. and radioactive waste, and a process for its production.
Abgebrannte Brennelemente aus Kernreaktoren müssen nach einer gewissen Zwischenlagerzeit einer Endbeseitigung zugeführt werden. Hierzu werden zwei Möglichkeiten diskutiert:
- - Die Wiederaufarbeitung der Brennelemente mit Rückführung des Brennstoffes in die Brennelementfertigung sowie Abtrennung, Konditionierung und Endlagerung der Spaltprodukte.
- - Die direkte Endlagerung der abgebrannten Brennelemente.
- - The reprocessing of the fuel elements with return of the fuel to the fuel element production as well as separation, conditioning and final storage of the fission products.
- - The direct disposal of the spent fuel.
In beiden Fällen muss durch eine geeignete, insbesondere korrosions- und auslaugbeständige Einbindematrix bzw. ein entsprechendes Behältermaterial dafür gesorgt werden, dass der eingelagerte hochaktive Abfall für tausend Jahre oder länger am Einlagerungsort verbleibt und nicht in die Biosphäre zurückgelangt.In both cases, a suitable, in particular corrosion and leach-resistant, binding matrix or a corresponding container material must ensure that the highly active waste that is stored remains at the storage location for a thousand years or more and does not return to the biosphere.
Die bei der Wiederaufarbeitung abgebrannter Brennelemente anfallenden radioaktiven Abfälle müssen für die Einlagerung in eine endlagerfähige Form gebracht werden. Wirtschaftlich erforderlich ist hierbei eine hohe Beladung mit Abfall. Dazu ist eine starke Volumenreduktion - beispielsweise durch Eindampfen - bereits vor dem Verfestigungsschritt notwendig.The radioactive waste generated during the reprocessing of spent fuel elements must be brought into a form suitable for disposal. A high level of waste is economically necessary. This requires a substantial volume reduction - for example by evaporation - before the solidification step.
Zur Verfestigung hochradioaktiver Abfälle sind mehrere Verfahren bekannt. Beispielsweise erfolgt zunächst eine Kalzination des Abfalls in einem Wirbelbett zwischen 350 und 900°C. Dabei wird ein Gemisch aus Oxiden erhalten, das als Pulver oder Granulat in eine glasartige oder keramische Matrix eingebunden und dadurch zu einem endlagerfähigen Produkt verfestigt wird.Several methods are known for solidifying highly radioactive waste. For example, the waste is first calcined in a fluidized bed between 350 and 900 ° C. A mixture of oxides is obtained which is incorporated as a powder or granulate in a glass-like or ceramic matrix and thereby solidified to form a product that can be disposed of.
Für die Einbettung von mittel- und schwachaktiven Abfällen sind Verfahren bekannt, nach denen die Abfallstoffe z.B. mit Bitumen erhitzt und einem Extrudiervorgang unterworfen werden. Dabei wird der radioaktive Abfall in die Bitumenmasse eingebunden, heiss in Fässer gefüllt und endgelagert.Methods are known for embedding medium and low-level waste, according to which the waste materials e.g. heated with bitumen and subjected to an extrusion process. The radioactive waste is incorporated into the bitumen mass, hot filled into barrels and finally stored.
Ein weiteres Verfahren besteht darin, die radioaktiven Abfälle in Zement bzw. Beton zu fixieren. Hierbei wird der Abfall üblicherweise in Form eines Salzkonzentrates oder Schlammes verarbeitet, der sich zu etwa 70 - 80 Gew. aus flüssigen und zu 20 - 30 Gew.-% aus festen Bestandtei= len zusammensetzt. Der Schlamm wird mit Zement gemischt und abbinden gelassen. Dieser Arbeitsschritt kann gege- b.enenfalls direkt in den Endlagerfässern durchgeführt werden.Another method is to fix the radioactive waste in cement or concrete. Here, the waste is usually processed in the form of a salt concentrate or slurry, which extends to about 70 - 30 wt .-% composed len of solid Bestandtei = - 80 percent of liquid and 20.. The slurry is mixed with cement and allowed to set. If necessary, this step can be carried out directly in the final storage casks.
Ferner sind Verfahren zur Konditionierung radioaktiver Abfälle bekannt, bei denen der Abfall in ein vorzugsweise bei Raumtemperatur polymerisierbares Harz eingemischt wird, und dann zu einem festen Block auspolymerisiert.Furthermore, methods for conditioning radioactive waste are known, in which the waste is preferably disposed of in a polymerizable resin is mixed in at room temperature, and then polymerized into a solid block.
Diese bekannten Verfahren weisen insbesondere für höhere Aktivitätskonzentrationen eine Reihe von Nachteilen auf. So erfolgt die Verglasung der Abfälle bei hohen Temperaturen, üblicherweise oberhalb 1 000°C. Bei dieser Temperatur sind bereits einige Salze flüchtig und müssen durch aufwendige Methoden, z.B. der Abgasreinigung, zurückgeführt werden. Dies betrifft insbesondere die aktiven Verbindungen des Cäsiums und des Rutheniums. Die Wärmeleitfähigkeit der Glasmatrix ist relativ gering. Um eine - durch die Nachwärme verursachte - unzulässige hohe Zentraltemperatur der Gebinde nicht zu überschreiten, sind daher Abfallkonzentration und Blockdurchmesser auf Werte von etwa 20 Gew.-% bzw. 20 bis 30 cm begrenzt. Weiterhin treten durch die Unterschiede der thermischen Ausdehnungskoeffizienten von Glas und Behältermaterial beim Abkühlen mechanische Spannungen auf, die zu unerwünschter Spannungskorrosion und Rissbildüng im Glas führen können. Die erforderliche Abkühlzeit für Glasabfallgebinde kann mehrere Tage betragen, um rissfreie Gebinde zu erzeugen. Dieser zusätzliche Verfahrensschritt erfordert daher teurenHeisszellenplatz.These known methods have a number of disadvantages, in particular for higher activity concentrations. The waste is glazed at high temperatures, usually above 1,000 ° C. At this temperature, some salts are already volatile and have to be processed using complex methods, e.g. exhaust gas purification. This applies in particular to the active compounds of cesium and ruthenium. The thermal conductivity of the glass matrix is relatively low. In order not to exceed an inadmissibly high central temperature of the containers caused by the residual heat, the waste concentration and block diameter are therefore limited to values of approximately 20% by weight or 20 to 30 cm. Furthermore, due to the differences in the thermal expansion coefficients of glass and container material, mechanical stresses occur during cooling, which can lead to undesirable stress corrosion and crack formation in the glass. The required cooling time for glass waste containers can take several days to produce crack-free containers. This additional process step therefore requires expensive hot cell space.
Die Bituminierung ist nur auf relativ niedrige Aktivitätskonzentrationen anwendbar, z.B. für den sogenannten flüssigen mittelaktiven Abfall von ca. 0,1 - 1 Ci β,δ-Aktivität. Es sind Temperaturen von 150 - 200°C notwendig, was aufwendige Sicherheitsvorkehrungen, z.B. gegen Brand, erfordert. Ausserdem bildet Bitumen unter Bestrahlung Radiolysegase, wie z.B. Wasserstoff.Bituminization is only applicable to relatively low activity concentrations, e.g. for the so-called liquid medium-active waste of approx. 0.1 - 1 Ci β, δ activity. Temperatures of 150 - 200 ° C are necessary, which requires complex safety precautions, e.g. against fire, required. In addition, under radiation, bitumen forms radiolysis gases, e.g. Hydrogen.
Die einfache Technik der Zementierung ist ebenfalls mit Nachteilen behaftet. So erhält man bei gleichen Abfallmengen grosse Abfallvolumina, z.B. gegenüber Bitumeneinbindung das 3- bis 5fache Volumen, ein durch die Porosität des Zements bedingtes relativ schlechtes Auslaugverhalten der eingeschlossenen radioaktiven Abfälle, und eine Radiolyse des im Zement gebundenen Wassers, welche zu relativ grossen Gasmengen, wie Wasserstoff, führen kann.The simple technique of cementing also has disadvantages. So you get large volumes of waste with the same amount of waste, e.g. 3 to 5 times the volume compared to bitumen inclusion, a relatively poor leaching behavior of the enclosed radioactive waste due to the porosity of the cement, and a radiolysis of the water bound in the cement, which can lead to relatively large amounts of gas, such as hydrogen.
Bei der Einbindung in polymerisierbare Harze werden grundsätzlich Kohlenwasserstoffverbindungen eingesetzt. Daher kann durch die Strahleneinwirkung des radioaktiven Abfalls die Sprödigkeit des Kunstharzes erhöht und damit die mechanische Integrität der Gebinde gefährdet werden. Auch für solche Formkörper gilt eine nur relativ geringe Radiolysebeständigkeit und die Freisetzung von Wasserstoff.When incorporated into polymerizable resins, hydrocarbon compounds are generally used. Therefore, the radiation of the radioactive waste can increase the brittleness of the synthetic resin and thus jeopardize the mechanical integrity of the container. Such molded articles also have only a relatively low resistance to radiolysis and the release of hydrogen.
Aus der DE-OS 27 56 700 ist ein Verfahren zur Einschliessung von radioaktivem Abfall in eine Metall-Matrix bekannt, die durch isostatisches Umpressen des Abfalls mit Metallpulver bei Temperaturen zwischen 1 000 und 1 500° C gebildet wird. Die hohen Presstemperaturen und der grosse Verbrauch an korrosionsbeständigem Metall lassen dieses Verfahren zumindest für grosse Köper und für die Einschliessung flüchtiger radioaktiver Stoffe als wenig geeignet erscheinen.From DE-OS 27 56 700 a method for enclosing radioactive waste in a metal matrix is known, which is formed by isostatic pressing of the waste with metal powder at temperatures between 1000 and 1500 ° C. The high pressing temperatures and the large consumption of corrosion-resistant metal make this process seem at least unsuitable for large bodies and for the inclusion of volatile radioactive substances.
Ausserdem sind sogenannte Endlagerbehälter bekannt, die die Abfallstoffe aufnehmen und zur Erzielung einer ausreichend langfristigen Korrosionsbeständigkeit meist als Mehrschichtbehälter ausgebildet sind. Als Behältermaterialien werden korrosionsfeste metallische und nichtmetallische Werkstoffe verwendet.In addition, so-called final storage containers are known which absorb the waste materials and are usually designed as multi-layer containers to achieve sufficient long-term corrosion resistance. Corrosion-resistant metallic and non-metallic materials are used as container materials.
In der DE-OS 29 17 437 ist ein Verfahren beschrieben, radioaktive und toxische Abfälle unter schonenden Bedingungen in eine gut wärmeleitende Kohlenstoffmatrix einzubinden, die aus einem Gemisch von pulverförmigem Kohlenstoff, vorzugsweise Graphit, mit einem Bindemittel besteht, wobei durch Verpressen mit dem zugemischten Abfall bei Temperaturen oberhalb 100°C ein entsprechender Formkörper gebildet wird. Als Bindemittel kommen organische und anorganische Stoffe in Betracht, von Vorteil ist die Verwendung von Schwefel und bei einer bevorzugten Ausführung wird ein Gemisch von Schwefel und Nickel eingesetzt, das bei einer Presstemperatur von etwa 400°C das in Wasser schwerlösliche Nickelsulfid bildet. Zwar ist diese Matrix korrosions- und auslaugbeständig, bei den nach dem angegebenen Mischverfahren unter Zumischung des Abfalls zu den Matrixausgangsstoffen hergestellten Formkörpern lassen sich die Abfallstoffe aber aus der Oberflächenschicht herauslösen.DE-OS 29 17 437 describes a process for incorporating radioactive and toxic waste into a good heat-conducting carbon matrix under mild conditions bind, which consists of a mixture of powdered carbon, preferably graphite, with a binder, wherein a corresponding shaped body is formed by pressing with the admixed waste at temperatures above 100 ° C. Suitable binders are organic and inorganic substances, the use of sulfur is advantageous and in a preferred embodiment a mixture of sulfur and nickel is used which forms the water-insoluble nickel sulfide at a pressing temperature of about 400 ° C. Although this matrix is resistant to corrosion and leaching, the waste materials can be removed from the surface layer in the case of the molded articles produced by adding the waste to the matrix starting materials.
Für eine wirtschaftliche Anwendung dieses Verfahrens ist eine möglichst hohe Konzentration an Abfall im. Formkörper erforderlich. Bei höheren Abfallanteilen im Formkörper wird aber der Abfall langfristig aus immer tieferen Schichten und schliesslich aus dem gesamten Formkörper ausgelaugt.For an economical application of this method, the highest possible concentration of waste is in the. Moldings required. In the case of higher proportions of waste in the molded article, the waste is leached out in the long term from ever deeper layers and ultimately from the entire molded article.
Es war daher Aufgabe der vorliegenden Erfindung, einen Formkörper aus Graphit und einem anorganischen Bindemittel zur sicheren Langzeit-Einbindung von radioaktiven und toxischen Abfällen zu schaffen, der hochdicht, korrosions-und auslaugbeständig ist, so dass die eingebundenen Abfälle auch in sehr langen Zeiträumen nicht herausgelöst werden können.It was therefore an object of the present invention to provide a shaped body made of graphite and an inorganic binder for the safe long-term incorporation of radioactive and toxic waste, which is highly dense, corrosion and leach-resistant, so that the incorporated waste does not dissolve even in very long periods of time can be.
Diese Aufgabe wurde erfindungsgemäss dadurch gelöst, dass der Formkörper aus einem Kern, in dem die Abfälle eingebettet sind, und aus einer abfallfreien Schale aus dem gleichen Material besteht.This object was achieved according to the invention in that the molded body consists of a core in which the waste is embedded and a waste-free shell made of the same material.
Die Graphitmatrix für Kern und Schale wird dabei in bekannter Weise durch Pressen eines Gemisches von pulverförmigem Graphit und einem anorganischen Bindemittel oder den Ausgangskomponenten eines anorganischen Bindemittels bei einer Temperatur oberhalb 100°C hergestellt. Als anorganisches Bindemittel wird entweder Schwefel oder ein stabiles Metallsulfid eingesetzt. Es ist vorteilhaft, als Graphit ein leicht verpressbares Naturgraphitpulver zu verwenden.The graphite matrix for core and shell is produced in a known manner by pressing a mixture of powdered graphite and an inorganic binder or the starting components of an inorganic binder at a temperature above 100 ° C. Either sulfur or a stable metal sulfide is used as the inorganic binder. It is advantageous to use an easily compressible natural graphite powder as graphite.
Bei Einsatz von Schwefel als Bindemittel wird eine Presstemperatur im Bereich der Schmelztemperatur des Schwefels von etwa 120 C sowie ein Pressdruck von 10 - 50 MN/m2, vorzugsweise etwa 20 MN/m2, verwendet. Ein so hergestellter Formkörper aus Kern und Schale ist geeignet für toxische und schwach radioaktive Abfälle, die nur geringe Eigenwärme erzeugen. In stärker radioaktivem Abfall tritt eine grössere Zerfallswärme auf, insbesondere bei hochaktivem Abfall, die eine hohe thermische Stabilität der Graphitmatrix erfordert.When using sulfur as a binder, a pressing temperature in the range of the melting temperature of the sulfur of approximately 120 ° C. and a pressing pressure of 10-50 MN / m 2 , preferably approximately 20 MN / m 2 , are used. A core and shell shaped body produced in this way is suitable for toxic and low-level radioactive waste which only generates a small amount of heat. Greater decay heat occurs in more radioactive waste, particularly in the case of highly active waste, which requires high thermal stability of the graphite matrix.
Der Zusatz von geeigneten Metall- oder Legierungspulvern zur Bildung.von stabilen Metallsulfiden ergibt sehr temperaturbeständige Bindemittel in der Graphitmatrix. Die chemische Reaktion zwischen Metall und Schwefel erfolgt in dem Gemisch aus Graphit, Schwefel und Metall-oder Legierungspulver durch Temperaturanhebung beim Pressen der Formkörper.The addition of suitable metal or alloy powders to form stable metal sulfides results in very temperature-resistant binders in the graphite matrix. The chemical reaction between metal and sulfur takes place in the mixture of graphite, sulfur and metal or alloy powder by raising the temperature when pressing the moldings.
Als Metalle können beispielsweise Blei, Eisen, Nickel, Kobalt, Kupfer, Molybdän, Vanadium oder Wolfram eingesetzt werden. Als besonders vorteilhaft hat sich die Verwendung von Nickel zur Ausbildung von Nickelsulfid erwiesen.For example, lead, iron, nickel, cobalt, copper, molybdenum, vanadium or tungsten can be used as metals. The use of nickel to form nickel sulfide has proven to be particularly advantageous.
Der Abfallanteil im Kern liegt vorteilhafterweise zwischen 1 und 70 Vol. %, vorzugsweise zwischen 10 und 50 Vol.%, so dass der Kern als mechanisch stabiler Körper vorliegt, der im wesentlichen die gleichen physikalischen Eigenschaften wie die abfallfreie Schale hat.The proportion of waste in the core is advantageously between 1 and 70% by volume, preferably between 10 and 50% by volume, so that the core is in the form of a mechanically stable body which has essentially the same physical properties as the waste-free shell.
Bei Verwendung von Schwefel als alleiniges Bindemittel reichen eine Presstemperatur von 130°C und ein Pressdruck von etwa 20 bis 50 MN/m2 aus, um einen hochdichten, korrosions- und auslaugbeständigen Formkörper zu erzeugen.When using sulfur as the sole binder, a pressing temperature of 130 ° C and a pressing pressure of about 20 to 50 MN / m 2 are sufficient to produce a high-density, corrosion and leach-resistant molded body.
Beim Einsatz von Nickelsulfid als Bindemittel für die Einbindung von stärker radioaktiven Abfallstoffen erfolgt die Verbindung zwischen Innenzone und Schale vorzugsweise bei einer Temperatur oberhalb 300°C und einem Pressdruck von 30 bis 100 MN/m2. Vorzugsweise wird der Kern zunächst ebenfalls bei Raumtemperatur oder bei erhöhter Temperatur vorgepresst und der Pressling in einen vorgepressten Hohlzylinder mit angefügtem Boden eingesetzt. Nach Auflegen der Deckelplatte wird der gesamte Formkörper bei einer Temperatur oberhalb 100°C gepresst und dabei auf über 80 % der theoretischen Dichte verdichtet. Unter anhaltendem Druck wird die Temperatur auf über 400°C erhöht, vorzugsweise auf etwa 440°C. Der nach Abkühlen auf unterhalb 400°C ausgestossene Formkörper hat eine Dichte oberhalb 90 % des theoretischen Wertes und ist hochdicht und frei von durchgehenden Poren.When using nickel sulfide as a binder for the incorporation of more radioactive waste materials, the connection between the inner zone and the shell is preferably carried out at a temperature above 300 ° C. and a pressure of 30 to 100 MN / m 2 . The core is preferably also initially pressed at room temperature or at elevated temperature and the compact is inserted into a pre-pressed hollow cylinder with an attached base. After placing the cover plate, the entire molded body is pressed at a temperature above 100 ° C and compressed to over 80% of the theoretical density. With continued pressure, the temperature is raised to above 400 ° C, preferably to about 440 ° C. The molded body, which is ejected after cooling to below 400 ° C., has a density above 90% of the theoretical value and is highly dense and free of continuous pores.
Der erfindungsgemässe Formkörper ist chemis ch ausserordentlich stabil, d.h. auch in stark korrosiven Medien noch sehr korrosions- und auslaugbeständig.The shaped body according to the invention is chemically extremely stable, i.e. still very corrosion and leach resistant even in highly corrosive media.
Der abfallhaltige Kern im Inneren der abfallfreien Schale hat weitgehend dieselben physikalisch-chemischen Kenndaten wie die Umhüllung, so dass mechanische Spannungen, die ein Reissen des Gebindes verursachen können, praktisch entfallen.The waste-containing core in the interior of the waste-free shell has largely the same physico-chemical characteristics as the casing, so that mechanical stresses that can cause the container to tear are practically eliminated.
Die Abbildung zeigt schematisch in beispielhafter Ausführungsform einen erfindungsgemässen Formkörper.The figure schematically shows a molded body according to the invention in an exemplary embodiment.
Der Kern (1) des zylindischen Formkörpers besteht aus einer Matrix aus Graphit mit anorganischem Bindemittel, in welche die körnigen oder stückigen radioaktiven Abfälle (2) eingelagert sind. Der Kern (1) ist allseits von der abfallfreien Schale (3) umgeben, mit der sie übergangsfrei verbunden ist. Gestrichelt sind die Stellen angegeben, an denen die Schale (3) aus vorgeformten ringförmigen Teilstücken (4) zusammengefügt ist. Zusätzlich ist die Schale (3) von einer Stahlhülle (5) umgeben.The core (1) of the cylindrical shaped body consists of a matrix of graphite with an inorganic binder, in which the granular or lumpy radioactive waste (2) is embedded. The core (1) is surrounded on all sides by the waste-free shell (3), with which it is connected without transition. The places where the shell (3) is assembled from preformed annular sections (4) are shown in dashed lines. In addition, the shell (3) is surrounded by a steel shell (5).
Der erfindungsgemässe Formkörper'soll anhand folgender Beispiele näher erläutert werden:The shaped body according to the invention is to be explained in more detail using the following examples:
Das für die Herstellung der Graphitmatrix verwendete Presspulver enthält folgende Komponenten:
- 43,3 Gew.-% Naturgraphitpulver, 20,0 Gew.-% Schwefel und 36,7.Gew.-% Nickelmetallpulver.
- 43.3% by weight of natural graphite powder, 20.0% by weight of sulfur and 36.7% by weight of nickel metal powder.
Zur Herstellung eines ringförmigen Segments mit den Abmessungen:
- Aussendurchmesser 450 mm, Innendurchmesser 300 mm, Höhe 200 mm, werden etwa 58 kg des intensiv gemischten und anschliessend granulierten Presspulvers in eine von aussen beheizbare ringförmige Pressmatrize gefüllt. Im Schmelzbereich des Schwefels - bei 130°C - wird das Granulat mit einem Druck von etwa 100 MN/m2 zusammengepresst, die Temperatur bei konstantem Pressdruck anschliessend auf ca. 450°C erhöht und dabei der Schwefel zum Nickelsulfid umgesetzt. Nach dem Abkühlen auf 350°C erfolgt das Ausstossen des hohlzylindrischen Formkörpers.
- Outside diameter 450 mm, inside diameter 300 mm, height 200 mm, about 58 kg of the intensively mixed and then granulated press powder are filled into an externally heatable press die. In the melting range of the sulfur - at 130 ° C - the granulate is pressed together with a pressure of about 100 MN / m 2 , the temperature is then increased to approx. 450 ° C at constant pressure and the sulfur is converted to nickel sulfide. After cooling to 350 ° C., the hollow cylindrical shaped body is ejected.
Auf dem beschriebenen Wege werden 4 ringförmige Segmente hergestellt, die anschliessend zu einem etwa 800 mm langen Hohlzylinder durch Pressen zusammengefügt werden. Dazu bedarf es einer Temperatur von 500 - 600°C und eines Druckes von 50 MN/m2, als verbindende Zwischenschicht dient jeweils ein mit geringen Mengen Naturgraphitpulver versetztes Nickel/Schwefel-Pulvergemisch (Stöchiometrieverhältnis 1 : 1), welches unter den angegebenen Bedingungen ebenfalls zum Nickelsulfid reagiert. Nach demselben Verfahren wird die aus Presspulver gleicher Zusammensetzung hergestellte Bodenplatte angefügt. Entsprechend wird eine Deckelplatte aus dem Presspulver hergestellt.In the way described, 4 ring-shaped segments are produced, which are then assembled into an approximately 800 mm long hollow cylinder by pressing. This requires a temperature of 500 - 600 ° C and a pressure of 50 MN / m 2 , a nickel / sulfur powder mixture (stoichiometric ratio 1: 1) mixed with small amounts of natural graphite powder (stoichiometric ratio 1: 1) serves as the connecting intermediate layer reacted to nickel sulfide. The base plate made of pressed powder of the same composition is added using the same procedure. Accordingly, a cover plate is made from the press powder.
In diesen behälterartigen Hohlraum wird ein Presskörper aus der gleichen Matrix, der 50 Vol. % Abfall enthält, eingesetzt. Danach wird die Deckelplatte aufgelegt und unter den gleichen Bedingungen, wie für die Segmente angegeben, mit dem Hohlzylinder zu einer geschlossenen Schale verbunden.A compact made of the same matrix and containing 50 vol.% Waste is inserted into this container-like cavity. The cover plate is then placed on and connected to the hollow cylinder to form a closed shell under the same conditions as specified for the segments.
Aus dem Formkörper werden folgende Eigenschaften ermittelt:
Zum Einbinden simulierter radioaktiver Abfälle in eine anorganisch gebundene Graphitmatrix wird das analog Beispiel 1 hergestellte pulverförmige Gemisch aus den Ausgangskomponenten der Graphitmatrix mit etwa der gleichen Menge Feedklärschlamm-Simulat gemischt, das aus Molybdän, Molybdän-(VI)-Oxid, Mangan, Mangan-(IV)-Oxid, Zirkon, Cäciumchlorid, Antimon-(III)-Oxid, Edelstahl- und Nickelpulver besteht. Dieses Gemisch wird in den bei Raumtemperatur vorgepressten einseitig verschlossenen Hohlzylinder aus Graphit-Nickel-Schwefel-Matrix überführt, welcher sich in einer von aussen beheizbaren Matrize befindet. Nach dem Auflegen der kalt vorgepressten Deckelplatte wird der gesamte Formkörper im Schmelzbereich des Schwefels - bei 130°C - mit einem Druck von etwa 100 MN/m2 zusammengepresst, die Temperatur bei konstantem Pressdruck auf 450°C erhöht und dabei der Schwefel zum Nickelsulfid umgesetzt. Nach dem Abkühlen auf ca- 350 C erfolgt das Ausstossen des simulathaltigen Formkörpers. An diesem Körper werden neben den in Beispiel 1 genannten physikal-ischen Eigenschaften insbesondere niedrige Cs-Auslaugraten beobachtet: 3 . 10-4- 5 · 10-6 cm/d.To incorporate simulated radioactive waste into an inorganically bound graphite matrix, the pulverulent mixture prepared in the same way as in Example 1 from the starting components of the graphite matrix is mixed with approximately the same amount of feed sludge simulate, which consists of molybdenum, molybdenum (VI) oxide, manganese, manganese ( IV) oxide, zirconium, calcium chloride, antimony (III) oxide, stainless steel and nickel powder. This mixture is transferred to the hollow cylinder made of graphite-nickel-sulfur matrix, which is pre-pressed at room temperature and is located in a die that can be heated from the outside. After placing the cold-pressed cover plate, the entire molded body in the melting range of the sulfur - at 130 ° C - is compressed with a pressure of about 100 MN / m 2 , the temperature is increased to 450 ° C at constant pressure and the sulfur is converted to nickel sulfide . After cooling to about 350 ° C., the molded article containing the simulate is ejected. In addition to the physical properties mentioned in Example 1, particularly low Cs leaching rates are observed on this body: 3. 10 -4 - 5 x 10 -6 c m / d.
Die pulverförmigen Matrixkomponenten Graphit, Schwefel und Nickel werden entsprechend Beispiel 1 zunächst intensiv miteinander gemischt. Dem dabei gebildeten Presspulver werden etwa 3 cm lange Abschnitte von Brennstabhülsen (Hülsendurchmesser aussen 10,75 mm; Wandstärke 0,68 mm) aus Zirkaloy-4 zugemischt. Der Gewichtsanteil der kompaktierten bzw. unkompaktierten Hülsen liegt bei 25 Gew.-%.The powdery matrix components graphite, sulfur and nickel are first mixed intensively in accordance with Example 1. About 3 cm long sections of fuel rod sleeves (sleeve diameter outside 10.75 mm; wall thickness 0.68 mm) made of Zirkaloy-4 are mixed into the press powder formed. The proportion by weight of the compacted or uncompacted sleeves is 25% by weight.
Das Hülsen-/Presspulvergemisch wird bei Raumtemperatur in einer schwimmenden Stahlmatrize (Durchmesser innen 50 mm) mit einem Druck von etwa 5 MN/m2 vorgepresst. Der dabei gebildete "Kern" (Durchmesser 50 mm, Höhe 80 mm) besitzt etwa 50 % der theoretischen Dichte.The sleeve / pressed powder mixture is pre-pressed at room temperature in a floating steel die (inner diameter 50 mm) with a pressure of about 5 MN / m 2 . The "core" formed (diameter 50 mm, height 80 mm) has about 50% of the theoretical density.
Anschliessend wird der vorgepresste "Kern" in einer heizbaren Pressform in die ebenfalls bei Raumtemperatur und mit Druck von 5 MN/m2 vorgeformten Teile der Schale eingesetzt; die Schale besteht aus Bodenplatte, Hohlzylinder mit 66 mm Aussendurchmesser und Deckelplatte. Nach Erwärmen auf 130°C wird der Formkörper mit einem Druck von 50 MN/m2 auf etwa 85 % der theoretischen Dichte verdichtet. Unter anhaltendem Druck wird der fast fertige Probenkörper auf eine Temperatur von etwa 440°C erwärmt. Dabei setzt sich das Nickel/Schwefel-Gemisch in das chemisch, mechanisch und thermisch wesentlich stabilere Nickelsulfid um. Gleichzeitig erhöht sich die Dichte auf über 90 % des theoretischen Wertes.The pre-pressed "core" is then inserted in a heatable press mold into the parts of the shell which have also been pre-shaped at room temperature and with a pressure of 5 MN / m 2 ; the shell consists of a base plate, a hollow cylinder with an outer diameter of 66 mm and a cover plate. After heating to 130 ° C, the molded body is compressed with a pressure of 50 MN / m 2 to about 85% of the theoretical density. The almost finished test specimen is heated to a temperature of around 440 ° C under constant pressure. The nickel / sulfur mixture converts into the chemically, mechanically and thermally much more stable nickel sulfide. At the same time, the density increases to over 90% of the theoretical value.
Nach einer etwa 10-minütigen Haltezeit bei der Reaktionstemperatur wird der fertige Probenkörper auf 350 - 400°C abgekühlt und ausgestossen (Durchmesser 66 mm, Höhe etwa 75 mm).After a holding time of approximately 10 minutes at the reaction temperature, the finished test specimen is cooled to 350-400 ° C. and ejected (diameter 66 mm, height approximately 75 mm).
Claims (9)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3144754 | 1981-11-11 | ||
DE19813144754 DE3144754A1 (en) | 1981-11-11 | 1981-11-11 | MOLDED BODY FOR INTEGRATING RADIOACTIVE WASTE AND METHOD FOR THE PRODUCTION THEREOF |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0081084A1 true EP0081084A1 (en) | 1983-06-15 |
Family
ID=6146107
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP82110144A Withdrawn EP0081084A1 (en) | 1981-11-11 | 1982-11-04 | Moulded body for encapsulating radioactive wastes, and process for manufacturing this body |
Country Status (7)
Country | Link |
---|---|
US (1) | US4600610A (en) |
EP (1) | EP0081084A1 (en) |
JP (1) | JPS58131598A (en) |
BR (1) | BR8206477A (en) |
DE (1) | DE3144754A1 (en) |
ES (1) | ES517241A0 (en) |
FI (1) | FI823529L (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010052321A1 (en) * | 2008-11-10 | 2010-05-14 | Ald Vacuum Technologies Gmbh | Matrix material composed of graphite and inorganic binders and suitable for final storage of radioactive waste, method for the manufacture thereof, and processing and use thereof |
US20100167905A1 (en) * | 2008-11-26 | 2010-07-01 | Ald Vacuum Technologies Gmbh | Matrix material comprising graphite and an inorganic binder suited for final disposal of radioactive waste, a process for producing the same and its processing and use |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3313251C2 (en) * | 1983-04-13 | 1986-03-06 | Hobeg Hochtemperaturreaktor-Brennelement Gmbh, 6450 Hanau | Process for preparing spherical fuel assemblies for final disposal |
US4900500A (en) * | 1987-01-20 | 1990-02-13 | Isolyser Co., Inc. | Point-of-use infectious waste disposal system |
US5360632A (en) * | 1993-08-10 | 1994-11-01 | Phillips Petroleum Company | Reduced leaching of arsenic and/or mercury from solid wastes |
US5569153A (en) * | 1995-03-01 | 1996-10-29 | Southwest Research Institute | Method of immobilizing toxic waste materials and resultant products |
US6010444A (en) * | 1997-09-05 | 2000-01-04 | Isolyser Company, Inc. | Infectious waste containment system |
US6017595A (en) * | 1997-09-15 | 2000-01-25 | Brenot; Stephen E. | Structural building materials or articles obtained from a composite including polymeric materials, solid waste material, and reinforcing materials |
WO2000077793A1 (en) * | 1999-06-14 | 2000-12-21 | Paul Scherrer Institut | Disposal of radioactive materials |
KR20030064033A (en) * | 2002-01-25 | 2003-07-31 | 주식회사 시스텍 | The nuclear fuel waste container for nuclear power plant |
DE102009044963B4 (en) * | 2008-11-10 | 2011-06-22 | ALD Vacuum Technologies GmbH, 63450 | Graphite matrix blocks with inorganic binder suitable for storage of radioactive waste and method of making the same |
DE102010003289B4 (en) * | 2010-03-25 | 2017-08-24 | Ald Vacuum Technologies Gmbh | Containers for the storage of radioactive waste and process for its production |
CN110095802B (en) * | 2018-01-31 | 2022-07-29 | 中国辐射防护研究院 | Method for simulating and researching hydrogen generation in radioactive solid waste disposal process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2441246A1 (en) * | 1978-11-09 | 1980-06-06 | Macedo Pedro | IMMOBILIZATION OF RADIOACTIVE WASTE IN GLASS CONTAINERS AND PRODUCTS THUS FORMED |
DE2917437A1 (en) * | 1979-04-28 | 1980-11-06 | Nukem Gmbh | METHOD FOR CONDITIONING RADIOACTIVE AND TOXIC WASTE |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4167491A (en) * | 1973-11-29 | 1979-09-11 | Nuclear Engineering Company | Radioactive waste disposal |
FR2375695A1 (en) * | 1976-12-21 | 1978-07-21 | Asea Ab | PROCESS FOR THE TREATMENT OF RADIOACTIVE WASTE |
SE414976B (en) * | 1977-12-20 | 1980-08-25 | Af Segerstad Peder Hard | LIST FOR FITTING A POSTER |
DE2942092C2 (en) * | 1979-10-18 | 1985-01-17 | Steag Kernenergie Gmbh, 4300 Essen | Final storage containers for radioactive waste, in particular irradiated nuclear reactor fuel elements |
US4328423A (en) * | 1980-04-23 | 1982-05-04 | The United States Of America As Represented By The United States Department Of Energy | Canister arrangement for storing radioactive waste |
-
1981
- 1981-11-11 DE DE19813144754 patent/DE3144754A1/en not_active Withdrawn
-
1982
- 1982-10-15 FI FI823529A patent/FI823529L/en not_active Application Discontinuation
- 1982-11-04 EP EP82110144A patent/EP0081084A1/en not_active Withdrawn
- 1982-11-09 US US06/440,314 patent/US4600610A/en not_active Expired - Fee Related
- 1982-11-09 BR BR8206477A patent/BR8206477A/en unknown
- 1982-11-10 JP JP57196162A patent/JPS58131598A/en active Pending
- 1982-11-10 ES ES517241A patent/ES517241A0/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2441246A1 (en) * | 1978-11-09 | 1980-06-06 | Macedo Pedro | IMMOBILIZATION OF RADIOACTIVE WASTE IN GLASS CONTAINERS AND PRODUCTS THUS FORMED |
DE2917437A1 (en) * | 1979-04-28 | 1980-11-06 | Nukem Gmbh | METHOD FOR CONDITIONING RADIOACTIVE AND TOXIC WASTE |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010052321A1 (en) * | 2008-11-10 | 2010-05-14 | Ald Vacuum Technologies Gmbh | Matrix material composed of graphite and inorganic binders and suitable for final storage of radioactive waste, method for the manufacture thereof, and processing and use thereof |
EA021732B1 (en) * | 2008-11-10 | 2015-08-31 | Алд Вакуум Текнолоджиз Гмбх | Matrix material composed of graphite and inorganic binders and suitable for final storage of radioactive waste, method for the manufacture thereof, and processing and use thereof |
US20100167905A1 (en) * | 2008-11-26 | 2010-07-01 | Ald Vacuum Technologies Gmbh | Matrix material comprising graphite and an inorganic binder suited for final disposal of radioactive waste, a process for producing the same and its processing and use |
US8502009B2 (en) * | 2008-11-26 | 2013-08-06 | Ald Vacuum Technologies Gmbh | Matrix material comprising graphite and an inorganic binder suited for final disposal of radioactive waste, a process for producing the same and its processing and use |
Also Published As
Publication number | Publication date |
---|---|
ES8404864A1 (en) | 1984-05-16 |
FI823529A0 (en) | 1982-10-15 |
ES517241A0 (en) | 1984-05-16 |
FI823529L (en) | 1983-05-12 |
BR8206477A (en) | 1983-09-27 |
DE3144754A1 (en) | 1983-05-19 |
US4600610A (en) | 1986-07-15 |
JPS58131598A (en) | 1983-08-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4297304A (en) | Method for solidifying aqueous radioactive wastes for non-contaminating storage | |
EP0081084A1 (en) | Moulded body for encapsulating radioactive wastes, and process for manufacturing this body | |
DE2917437A1 (en) | METHOD FOR CONDITIONING RADIOACTIVE AND TOXIC WASTE | |
EP2550664B1 (en) | Process for the production of packing for disposal of waste | |
EP2347422A1 (en) | Matrix material composed of graphite and inorganic binders and suitable for final storage of radioactive waste, method for the manufacture thereof, and processing and use thereof | |
DE3214242A1 (en) | METHOD FOR IMPROVING THE PROPERTIES OF RADIOACTIVE WASTE REINFORCEMENTS REQUIRED FOR LONG TERM STORAGE | |
EP0168638B1 (en) | Process for making disposable products from polluting salt mixtures | |
EP0082267B1 (en) | Moulded body for encapsulating radioactive wastes, and process for manufacturing this body | |
GB2041912A (en) | Moulded bodies containing radioactive waste | |
EP0081660B1 (en) | Moulded body for encapsulating spent nuclear fuel elements, and process for manufacturing this body | |
DE102009044963B4 (en) | Graphite matrix blocks with inorganic binder suitable for storage of radioactive waste and method of making the same | |
EP0054604B1 (en) | Process for preparing spent solid bodies for the final disposal of radioactive wastes | |
US4482481A (en) | Method of preparing nuclear wastes for tansportation and interim storage | |
DE3219114C2 (en) | ||
DE2945006A1 (en) | METHOD FOR PRODUCING HIGH-RADIOACTIVE WASTE MATERIALS CONTAINING | |
DE102012112648B4 (en) | Graphite matrix with crystalline binder | |
DE3018745C2 (en) | Method for embedding tritium or tritium-containing radioactive gases | |
DE3018746C2 (en) | Process for embedding tritiated waste | |
DE10229697A1 (en) | A process for stabilization of solid waste with immobilization of the waste by encapsulation useful for stabilization of solid waste, e.g. chemical and radioactive waste material prior to disposal | |
DE2855738C3 (en) | Process for the production of storable, biologically harmful, in particular radioactive, waste | |
DE3212507A1 (en) | Casks for the storage of radioactive substances having a ceramic corrosion-protective layer surrounding the substances | |
DE102010000974A1 (en) | Form stable body for use as neutron absorber rod in transport container for transporting and/or storing e.g. fuel element in research plant in nuclear power station, has neutron absorber reacted to carbide in elementary form | |
DE1514223C (en) | Radioactive radiation source and processes for their production | |
DE102012112642A1 (en) | Graphite matrix, useful for manufacturing a molded body to store radioactive waste, comprises graphite and glass ceramic | |
AT263703B (en) | Process for producing carbon bodies |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19821104 |
|
AK | Designated contracting states |
Designated state(s): BE CH DE FR GB LI SE |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
|
18W | Application withdrawn |
Withdrawal date: 19850427 |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: HUSCHKA, HANS, DR. DIPL.-CHEM. Inventor name: RACHOR, LOTHAR, ING. Inventor name: SCHMIDT-HANSBERG, DR. DIPL.-CHEM. Inventor name: KROEBEL, REINHARD, DR. DIPL.-CHEM. Inventor name: HROVAT, MILAN, DR. DIPL.-ING. |