EP0204634A1 - Verfahren und Einrichtung zum Behandeln von nichtorganischen festen Tritium enthaltenden Abfällen - Google Patents
Verfahren und Einrichtung zum Behandeln von nichtorganischen festen Tritium enthaltenden Abfällen Download PDFInfo
- Publication number
- EP0204634A1 EP0204634A1 EP86401184A EP86401184A EP0204634A1 EP 0204634 A1 EP0204634 A1 EP 0204634A1 EP 86401184 A EP86401184 A EP 86401184A EP 86401184 A EP86401184 A EP 86401184A EP 0204634 A1 EP0204634 A1 EP 0204634A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- waste
- gases
- detritiation
- hydrogen
- tank
- 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.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 15
- 239000007787 solid Substances 0.000 title claims abstract description 6
- 230000008569 process Effects 0.000 title abstract description 4
- 239000007789 gas Substances 0.000 claims abstract description 37
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 21
- 239000001257 hydrogen Substances 0.000 claims abstract description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 230000008018 melting Effects 0.000 claims abstract description 16
- 238000002844 melting Methods 0.000 claims abstract description 16
- 239000002808 molecular sieve Substances 0.000 claims abstract description 12
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 12
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 230000003647 oxidation Effects 0.000 claims abstract description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 9
- 230000005587 bubbling Effects 0.000 claims abstract description 5
- 230000004927 fusion Effects 0.000 claims description 14
- 238000000605 extraction Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 description 16
- 229910052722 tritium Inorganic materials 0.000 description 16
- XLYOFNOQVPJJNP-PWCQTSIFSA-N Tritiated water Chemical compound [3H]O[3H] XLYOFNOQVPJJNP-PWCQTSIFSA-N 0.000 description 8
- 238000005086 pumping Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000007872 degassing Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- YZCKVEUIGOORGS-OUBTZVSYSA-N Deuterium Chemical compound [2H] YZCKVEUIGOORGS-OUBTZVSYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 229910052805 deuterium Inorganic materials 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000005496 eutectics Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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
- G21F9/308—Processing by melting the waste
-
- 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
- G21F9/02—Treating gases
Definitions
- the subject of the present invention is a method and a device for the treatment of non-organic solid waste having been in contact with tritium or having contained tritiated products.
- the present invention specifically relates to a process for treating tritiated waste which is simple and easy to implement and which makes it possible to considerably reduce the tritium content of the treated parts. It also makes it possible to homogenize the residual content, which facilitates the measurement of this content.
- Gas extraction can be done in several ways.
- Another method consists in injecting hydrogen into the mass of molten waste, while constantly extracting the atmosphere contained in the enclosure.
- hydroxide designates all the isotopes of this element, that is to say hydrogen as well as deuterium or tritium.
- the oxidation of these elements therefore makes it possible to obtain either water, or heavy water, or tritiated water, or a mixture of the different molecular species.
- the role of the molecular sieve is to retain the water molecules formed during contact with the oxidation catalyst, which makes it possible to trap, among other things, tritiated water. This is then subjected to further processing.
- the airlock is in the form of a bell that can pivot relative to the tank.
- the device may also include means for bubbling hydrogen through the mass of molten waste.
- the means for evacuating the furnace and bringing the gases released during the melting to the detritiation unit comprise at least one pumping group connected to the tank of the furnace by a first pipe and to the detritiation assembly by a second pipe.
- This pumping group can be a combination of primary pumps and / or secondary pumps. It must be particularly tight vis-à-vis the outside and contain the minimum of organic materials, in particular the minimum of lubricating oil or grease in the parts in contact with the fluid. This relates more particularly to gaseous tritium, tritiated water vapor and possibly tritiated hydrocarbons.
- the device which is the subject of the invention firstly comprises an oven, bearing the general reference 2, placed inside a glove box 4.
- This oven is essentially constituted a tank 6 arranged horizontally and open at its upper part.
- this tank is made of double-walled stainless steel and is cooled by a circulation of water.
- a crucible 12 of refractory material which contains the tritiated waste 14. These are heated by induction thanks to - a coil 16 when their nature allows. If it is aluminum waste, a graphite crucible can be used to achieve electromagnetic coupling. In this case, the temperature of the liquid mass is of the order of 900 ° C.
- the liquid mass is at a temperature of the order of 1600 ° C.
- graphite can be added to the waste in order to facilitate the realization of the electromagnetic coupling.
- carbon can combine with iron to give a carbide whose melting point is lower than that of stainless steel.
- the tank 6 is closed by a vacuum valve 18, which is surmounted by an airlock 20 used for the introduction of the products to be treated.
- the airlock 20 is in the form of a bell open downwards and able to pivot around an axis 22.
- the airlock is thus movable between an open position 20a shown in dashed lines in the figure and a closed position 20b shown in solid lines.
- a nacelle 13 containing the waste is introduced inside the airlock from below, when the latter is in the open position, thanks to a cable 24.
- an ingot mold '15 in which the liquid contained in the crucible 12 is poured once the latter is filled. This facilitates the release of the ingot once solidified.
- the mold is filled by pivoting the crucible 12.
- a pipe 26 equipped with a valve 28 places the tank 6 of the oven in communication with a pumping assembly 30 which, in the example shown here, comprises a primary pump 32 and a secondary pump 34.
- a pumping assembly 30 which, in the example shown here, comprises a primary pump 32 and a secondary pump 34.
- These pumps allow on the one hand to create a vacuum inside the furnace and, on the other hand, to send the gases released during the melting of the waste 14 to the detritiation unit 36 which will be described later in the remainder of this text.
- the primary pump 32 or the secondary pump 34 is used, depending on whether one wishes to obtain a more or less high vacuum. It is also possible to sweep the tank 6 with an appropriate gas, for example argon, hydrogen, dry air or helium.
- a compressed gas bottle 17 placed outside the glove box 4 and connected to the tank 6 by a pipe 19 while the pumping group 30 remains on the way in order to constantly extract the gases contained in the enclosure 6.
- it can be maintained under a reduced pressure of the order of 300 millibars, or under a primary vacuum, the pressure being less than 1 millibar.
- it is also possible, while carrying out such a sweep, to inject hydrogen into the mass of molten waste 14, for example by means of a hydrogen bottle 21 placed outside the glove box 4 and connected to the crucible 12 by a pipe 23.
- An isotope dilution is thus carried out: the content of isotopes of hydrogen isotopes remaining constant, if hydrogen is introduced by bubbling, the hydrogen content is increased and the tritium content is reduced .
- This method therefore has the effect of accelerating detritiation, especially since the excess hydrogen entrains the tritium which is thus released.
- the pumping assembly 30 is connected to the detritiation assembly 36 by a pipe 38 fitted with a valve 40.
- the pipe 38 opens into a container 42, which contains an oxidation catalyst 46 This may be, for example, a product from the Deoxo series marketed by the ENGEL-HARD Company.
- a pipe 48 connects the container 42 to two containers 50 placed in parallel and each containing a molecular sieve 52.
- the gases having passed through the detritiation assembly 36 and exiting at the bottom of the containers 50 are extracted through a pipe 54 connected to an extraction device.
- a regeneration device 53 comprises a cold trap and a circulation pump. It allows a counter-current circulation of dry air in the molecular sieves. This is how the dry air goes from the regenerator 53 to the bottom of the containers 50, passes through the molecular sieves 52 from bottom to top and returns to the regenerator 53 by a pipe 57.
- the line 48 is equipped with a heat exchanger 49 in order to cool the gases leaving the container 42 containing the oxidation catalyst 46.
- the airlock is then emptied by means of the pumping group.
- the vacuum valve is withdrawn and the airlock is in direct communication with the tank 6.
- the basket 13 is then lowered inside the crucible 12.
- the main advantage of the airlock is that it allows the successive introduction of several charges without stopping the heating means and without breaking the vacuum.
- the waste to be treated when placed in bulk, occupies a significant volume since it is essentially containers, pipes, taps, valves, etc. When they are melted, the mass in fusion (and therefore the solid mass that will result after solidification) is much more compact and occupies only part of the volume of the crucible. This is why it is possible to carry out several loads during the same operation in order to completely fill the crucible 12.
- the tank 6 of the oven is closed in leaktight manner by the valve at vacuum 18 and the vacuum still prevails inside the tank.
- the nacelle itself melts with the waste and that it is therefore preferable to make it from a light and inexpensive material whose melting point is compatible with that of the waste to be treated.
- the gases contained in the enclosure 6 are permanently extracted, the gases contained in the products 14 are continuously released during the melting and are evacuated by means of the pumping group 30.
- tritium is a gas and the Tritiated water vaporizes, this has the effect of removing most of the tritium or tritiated water absorbed in the waste.
- the gases are sent, through the pipe 38, to the container 42. During their passage through this container, they are in contact with the oxidation catalyst 46, which has the effect of oxidizing the isotopes of hydrogen and in particular to transform tritium into tritiated water.
- This tritiated water which is in the form of vapor, then passes along the pipe 48 and passes through the containers 50 which contain the molecular sieves 52. During the passage of the gases through these molecular sieves, these retain all the vapor of water, and therefore tritiated water which will then undergo a special treatment.
- the method and the device which are the subject of the invention have particularly advantageous advantages, the main one of which is that they make it possible to obtain a metallic mass in which the level of tritium (and therefore the activity) has been considerably reduced. This is primarily due to the fact that most of the tritium was removed with the gases during the melting. On the other hand, the waste which initially occupied a large volume and had a large contact surface with air, is found, after fusion and solidification, in the form of a compact mass of small volume and having a contact surface. with little importance. As the degassing rate of the tritiated compounds is proportional to the surface, this rate is considerably reduced by the transformation of a mass of waste into a compact and homogeneous mass. In addition, while in the pipes, valves, containers from the dismantling of the factory, the contamination is extremely variable, the latter is homogeneous in the solid mass obtained after the fusion. We can therefore know the contamination rate by making a single measurement.
Landscapes
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Processing Of Solid Wastes (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8508666A FR2583208B1 (fr) | 1985-06-07 | 1985-06-07 | Procede et dispositif pour le traitement de dechets trities solides non organiques |
FR8508666 | 1985-06-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0204634A1 true EP0204634A1 (de) | 1986-12-10 |
EP0204634B1 EP0204634B1 (de) | 1990-05-23 |
Family
ID=9320007
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19860401184 Expired - Lifetime EP0204634B1 (de) | 1985-06-07 | 1986-06-03 | Verfahren und Einrichtung zum Behandeln von nichtorganischen festen Tritium enthaltenden Abfällen |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0204634B1 (de) |
JP (1) | JPS61284697A (de) |
DE (1) | DE3671563D1 (de) |
ES (1) | ES8801473A1 (de) |
FR (1) | FR2583208B1 (de) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2620262A1 (fr) * | 1987-09-09 | 1989-03-10 | Commissariat Energie Atomique | Procede et installation de traitement de dechets organiques solides contamines par du tritium |
DE3930420C1 (en) * | 1989-09-12 | 1990-11-22 | Bundesrepublik Deutschland, Vertreten Durch Den Bundesminister Der Verteidigung, Dieser Vertreten Durch Den Praesidenten Des Bundesamtes Fuer Wehrtechnik Und Beschaffung, 5400 Koblenz, De | Radioactive waste tritium sepn. - by flushing in gas flow with oxygen, heating and passing tritium through water |
DE4029222C1 (en) * | 1990-09-14 | 1991-08-22 | Bundesrepublik Deutschland, Vertreten Durch Den Bundesminister Der Verteidigung, Dieser Vertreten Durch Den Praesidenten Des Bundesamtes Fuer Wehrtechnik Und Beschaffung, 5400 Koblenz, De | Economical and efficient tritium sepn. - involves passing gas to molten electrodes to ionise molecules, wash tower for absorption and condensate prodn. |
EP0503557A1 (de) * | 1991-03-13 | 1992-09-16 | Europäische Atomgemeinschaft (Euratom) | Verfahren zum Aufarbeiten von Absorberstäben aus wassergekühlten Kernreaktoren |
FR2974444A1 (fr) * | 2011-04-21 | 2012-10-26 | Commissariat Energie Atomique | Dispositif et procede de detritiation |
WO2021064304A1 (fr) | 2019-10-03 | 2021-04-08 | Onet Technologies Cn | Procédé pour décontaminer une pièce métallique contenant un gaz par irradiation laser dans un milieu liquide |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1400531B1 (it) * | 2010-06-22 | 2013-06-11 | Commissariat Energie Atomique | Processo per la detriziazione di soft housekeeping waste e impianto relativo |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1096072A (en) * | 1964-02-27 | 1967-12-20 | Atomic Energy Authority Uk | Improvements in or relating to incinerators |
DE2434876A1 (de) * | 1973-08-27 | 1975-04-03 | Engelhard Min & Chem | Verfahren und vorrichtung zum entfernen von tritium und tritiumverbindungen aus gasstroemen |
US4285891A (en) * | 1979-12-31 | 1981-08-25 | Exxon Nuclear, Inc. | Method of removing fission gases from irradiated fuel |
EP0036961A2 (de) * | 1980-03-26 | 1981-10-07 | Forschungszentrum Jülich Gmbh | Behälter zur Lagerung von Tritium |
-
1985
- 1985-06-07 FR FR8508666A patent/FR2583208B1/fr not_active Expired - Lifetime
-
1986
- 1986-06-03 DE DE8686401184T patent/DE3671563D1/de not_active Expired - Lifetime
- 1986-06-03 EP EP19860401184 patent/EP0204634B1/de not_active Expired - Lifetime
- 1986-06-06 ES ES555832A patent/ES8801473A1/es not_active Expired
- 1986-06-06 JP JP61130465A patent/JPS61284697A/ja active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1096072A (en) * | 1964-02-27 | 1967-12-20 | Atomic Energy Authority Uk | Improvements in or relating to incinerators |
DE2434876A1 (de) * | 1973-08-27 | 1975-04-03 | Engelhard Min & Chem | Verfahren und vorrichtung zum entfernen von tritium und tritiumverbindungen aus gasstroemen |
US4285891A (en) * | 1979-12-31 | 1981-08-25 | Exxon Nuclear, Inc. | Method of removing fission gases from irradiated fuel |
EP0036961A2 (de) * | 1980-03-26 | 1981-10-07 | Forschungszentrum Jülich Gmbh | Behälter zur Lagerung von Tritium |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2620262A1 (fr) * | 1987-09-09 | 1989-03-10 | Commissariat Energie Atomique | Procede et installation de traitement de dechets organiques solides contamines par du tritium |
EP0307306A1 (de) * | 1987-09-09 | 1989-03-15 | Commissariat A L'energie Atomique | Verfahren und Vorrichtung zur Behandlung von mit Tritium kontaminierten festen organischen Abfällen |
US4882093A (en) * | 1987-09-09 | 1989-11-21 | Commissariat A L'energie Atomique | Process and installation for the treatment of solid organic waste contaminated by tritium |
DE3930420C1 (en) * | 1989-09-12 | 1990-11-22 | Bundesrepublik Deutschland, Vertreten Durch Den Bundesminister Der Verteidigung, Dieser Vertreten Durch Den Praesidenten Des Bundesamtes Fuer Wehrtechnik Und Beschaffung, 5400 Koblenz, De | Radioactive waste tritium sepn. - by flushing in gas flow with oxygen, heating and passing tritium through water |
DE4029222C1 (en) * | 1990-09-14 | 1991-08-22 | Bundesrepublik Deutschland, Vertreten Durch Den Bundesminister Der Verteidigung, Dieser Vertreten Durch Den Praesidenten Des Bundesamtes Fuer Wehrtechnik Und Beschaffung, 5400 Koblenz, De | Economical and efficient tritium sepn. - involves passing gas to molten electrodes to ionise molecules, wash tower for absorption and condensate prodn. |
EP0503557A1 (de) * | 1991-03-13 | 1992-09-16 | Europäische Atomgemeinschaft (Euratom) | Verfahren zum Aufarbeiten von Absorberstäben aus wassergekühlten Kernreaktoren |
WO1992016948A1 (de) * | 1991-03-13 | 1992-10-01 | Europäische Atomgemeinschaft (Euratom) | Verfahren zum aufarbeiten von absorberstäben aus wassergekühlten kernreaktoren |
FR2974444A1 (fr) * | 2011-04-21 | 2012-10-26 | Commissariat Energie Atomique | Dispositif et procede de detritiation |
WO2012146861A3 (fr) * | 2011-04-21 | 2012-12-20 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Dispositif et procédé de détritiation |
RU2567020C2 (ru) * | 2011-04-21 | 2015-10-27 | Коммиссариа А Л'Энержи Атомик Э Оз Энержи Альтернатив | Устройство и способ детритирования |
WO2021064304A1 (fr) | 2019-10-03 | 2021-04-08 | Onet Technologies Cn | Procédé pour décontaminer une pièce métallique contenant un gaz par irradiation laser dans un milieu liquide |
FR3101558A1 (fr) | 2019-10-03 | 2021-04-09 | Onet Technologies Cn | Procédé pour décontaminer une pièce métallique contenant un gaz par irradiation laser dans un milieu liquide |
Also Published As
Publication number | Publication date |
---|---|
ES555832A0 (es) | 1987-12-16 |
ES8801473A1 (es) | 1987-12-16 |
FR2583208A1 (fr) | 1986-12-12 |
JPS61284697A (ja) | 1986-12-15 |
FR2583208B1 (fr) | 1992-04-24 |
EP0204634B1 (de) | 1990-05-23 |
DE3671563D1 (de) | 1990-06-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
FR2653694A1 (fr) | Procedes et appareil pour la coulee de metaux par contre-gravite, notamment de metaux reactifs, avec l'air. | |
EP0204634B1 (de) | Verfahren und Einrichtung zum Behandeln von nichtorganischen festen Tritium enthaltenden Abfällen | |
EP0012074B1 (de) | Verfahren zur Reinigung einer Kaltfangvorrichtung für flüssige Metalle und Vorrichtung zur Durchführung dieses Verfahrens | |
EP0255450B1 (de) | Vorrichtung zur Gasschützung eines flüssigen Metallgiessstrahls | |
EP0002664A1 (de) | Verfahren und Vorrichtung zum Behandeln von metallischem Schrott | |
CA1139970A (fr) | Procede et installation de fabrication de poudre metallique a partir d'un metal ou alliage en fusion | |
EP0196242A1 (de) | Verfahren zum Schützen eines Stahlgiessstrahls | |
FR2503598A1 (fr) | Appareil et procede pour fondre et traiter des residus metalliques | |
US5298196A (en) | Method and apparatus for extracting tritium and preparing radioactive waste for disposal | |
EP0125173B1 (de) | Verfahren zur Herstellung erstarrter Metallkörper aus der Schmelze eines Metalls | |
EP2700078B1 (de) | Vorrichtung und verfahren zum entfernen von tritium | |
EP0032343B1 (de) | Verfahren zur Gasspülung eines Metallschmelzbades | |
FR2548820A1 (fr) | Procede pour remplir des recipients metalliques d'une masse vitreuse fondue radioactive et dispositif de reception d'une masse vitreuse fondue radioactive | |
FR2705103A1 (fr) | Procédé et installation pour le traitement par thermolyse sous vide de produits solides, avec séparation et récupération en continu d'une fraction liquide de ces produits. | |
BE1006163A4 (fr) | Procede de traitement thermique d'objets metalliques sous atmosphere de protection. | |
FR2869028A1 (fr) | Procede et installation de fabrication de blocs d'un materiau semiconducteur | |
CA2093788C (fr) | Procede d'extraction du zinc present dans la fonte liquide, moyens en vue de la mise en oeuvre du procede et produits ainsi obtenus | |
EP0028569B1 (de) | Verfahren zum Spülen einer Metallschmelze durch Einblasen von Gas | |
FR2852608A1 (fr) | Procede et installation de recuperation du zinc contenu dans un bain de fonte liquide | |
NO132527B (de) | ||
CH518235A (fr) | Procédé et dispositif de purification isotopique de l'eau lourde | |
BE1005461A3 (fr) | Procede et installation d'affinage de ferromanganese carbure. | |
FR2816529A1 (fr) | Procede de traitement de residus d'incineration et installation pour la mise en oeuvre d'un tel procede | |
BE543396A (de) | ||
FR2516939A1 (fr) | Procede et installation pour le traitement de fonte hors four et fonte ainsi traitee |
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 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE CH DE GB IT LI LU NL SE |
|
17P | Request for examination filed |
Effective date: 19870509 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: COMMISSARIAT A L'ENERGIE ATOMIQUE |
|
17Q | First examination report despatched |
Effective date: 19881213 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE CH DE GB IT LI LU NL SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19900523 |
|
REF | Corresponds to: |
Ref document number: 3671563 Country of ref document: DE Date of ref document: 19900628 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19900630 |
|
ITF | It: translation for a ep patent filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
NLV1 | Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19910610 Year of fee payment: 6 |
|
ITTA | It: last paid annual fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19920630 Ref country code: CH Effective date: 19920630 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19930608 Year of fee payment: 8 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19940604 |
|
EUG | Se: european patent has lapsed |
Ref document number: 86401184.6 Effective date: 19950110 |
|
EUG | Se: european patent has lapsed |
Ref document number: 86401184.6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19950607 Year of fee payment: 10 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Effective date: 19960630 |
|
BERE | Be: lapsed |
Owner name: COMMISSARIAT A L'ENERGIE ATOMIQUE Effective date: 19960630 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20010530 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20010615 Year of fee payment: 16 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20020603 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030101 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20020603 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20050603 |