EP0355514A2 - Procédé pour conditionner les lessives radioactives d'évaporation provenant d'installations nucléaires - Google Patents
Procédé pour conditionner les lessives radioactives d'évaporation provenant d'installations nucléaires Download PDFInfo
- Publication number
- EP0355514A2 EP0355514A2 EP89114316A EP89114316A EP0355514A2 EP 0355514 A2 EP0355514 A2 EP 0355514A2 EP 89114316 A EP89114316 A EP 89114316A EP 89114316 A EP89114316 A EP 89114316A EP 0355514 A2 EP0355514 A2 EP 0355514A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- evaporator
- final storage
- concentrate
- repository
- storage container
- 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- Withdrawn
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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
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/08—Processing by evaporation; by distillation
Definitions
- the present invention relates to a method for conditioning radioactive evaporator liquors, optionally together with spherical resins, diatomaceous earth and filter aids from nuclear plants for the purpose of confinement by disposal in a heatable repository package.
- Radioactive evaporator liquors or mixtures of evaporator liquors with spherical resins, diatomaceous earth and filter aids are usually already used in the nuclear facilities, e.g. in nuclear power plants, concentrated to a dry matter content of approx. 20-25% by weight. They have to be concentrated further by evaporation in order to prepare them for disposal in appropriate containers.
- DE-PS 32 00 331 describes a process by which evaporator concentrates are dried in a heated repository vessel. Disadvantages of this process, however, are the relatively low evaporation rate and the formation of cavities, some of which are of considerable size, which are also distributed irregularly in the solidified product. This results in poor utilization of the container volume and an unfavorable economy.
- DE-OS 3544270 describes a drying process in which microwave energy is used for drying, liquids and solutions being sprayed into the container and solidified in one step. This process is very complex and therefore has economic disadvantages.
- This object is achieved in that the liquor or the mixture is first concentrated to 60 to about 85% by weight dry matter content in an evaporator, then the still flowable concentrate is poured into the heatable final storage container, and finally the concentrate in the final storage container at least the maximum temperature occurring in the repository is heated and the steam produced is suctioned off under reduced pressure until a solid floor body with a smooth surface has formed.
- the concentrate is preferably heated to the maximum temperature occurring in the repository.
- radioactive evaporator liquor (11), spherical resins (12) and filter aids (13) from nuclear power plants or other nuclear facilities are conveyed into an evaporator (1) which is operated with a stirrer (9) , a droplet separator (10), a condenser (7) and a distillate collector (8) is provided, from which the distillate can be removed in a controlled manner.
- the mixture (3) is heated with stirring and concentrated until the concentrate contains 60 to about 85% by weight of dry substance.
- the residual water still present in the concentrate which is viscous at the evaporator temperature and solid at room temperature, consists essentially of water of crystallization of the salt component.
- the viscous concentrate is then discharged in portions into a final storage container (2) provided with a heater (4).
- the first portion (5) is heated by the supply of heat as long and so high that the crystal water content is expelled from the concentrate to such an extent that a solid monolithic soil body with a smooth surface and without powdery components forms in the final storage container (2).
- This floor must remain firm even at the maximum temperature occurring in the repository, so that the evaporation temperature in the repository package (2) must be at least as high as the maximum temperature to be expected in the repository. Evaporation temperatures of about 70 ° C.
- a boiling water reactor-simulate mixture of evaporator liquors, ion exchanger spherical resins and filter aids was first concentrated in an evaporator.
- the resulting concentrate had the composition: Na2SO4 50% by weight Spherical resins 15% by weight Na3PO4 5% by weight Ca3 (PO4) 2 1.5% by weight Fe2O3 1.5% by weight Other 2.0% by weight Residual water 25% by weight
- This concentrate was drained in portions into a heated repository and solidified at 80 o C at 300 HPa.
- the end product had a residual water content of about 8% and had a microporous structure without voids and inhomogeneities.
- the end product surface was smooth, the abrasion and pressure resistance good.
- the geometric shape did not change during acceleration tests. Heating tests at 70 o C, which correspond to final storage conditions, showed that the solidification product did not change its consistency.
Landscapes
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Fertilizers (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19883827897 DE3827897A1 (de) | 1988-08-17 | 1988-08-17 | Verfahren zum konditionieren von radioaktiven verdampferlaugen aus kerntechnischen anlagen |
DE3827897 | 1988-08-17 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0355514A2 true EP0355514A2 (fr) | 1990-02-28 |
EP0355514A3 EP0355514A3 (fr) | 1991-12-27 |
Family
ID=6361022
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19890114316 Withdrawn EP0355514A3 (fr) | 1988-08-17 | 1989-08-03 | Procédé pour conditionner les lessives radioactives d'évaporation provenant d'installations nucléaires |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0355514A3 (fr) |
DE (1) | DE3827897A1 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995026556A1 (fr) * | 1994-03-25 | 1995-10-05 | British Nuclear Fuels Plc | Sechage de dechets radioactifs ou toxiques humides ou d'autres dechets humides dangereux |
ES2184540A1 (es) * | 1999-10-26 | 2003-04-01 | Equipos Nucleares Sa | Procedimiento para tratamiento de residuos liquidos radiactivos y su almacenamiento posterior. |
EP2733704A3 (fr) * | 2012-11-16 | 2016-06-29 | Hartmut Grunau | Récipient de stockage final et procédé de séchage d'objets contaminés dans un récipient de stockage final ainsi que procédé de fabrication de celui-ci |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19913103C1 (de) * | 1999-03-23 | 2000-12-14 | Kernkraftwerke Gundremmingen B | Verfahren und Vorrichtung zur Aufbereitung von Verdampferkonzentraten aus kerntechnischen Anlagen |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1614497A1 (de) * | 1967-04-12 | 1970-08-20 | Siemens Ag | Verfahren zur Konzentrierung radioaktiver Abfaelle |
FR2307342A1 (fr) * | 1975-04-11 | 1976-11-05 | Licentia Gmbh | Procede de traitement de concentres radioactifs |
GB2113902A (en) * | 1982-01-08 | 1983-08-10 | Nuklear Service Gmbh Gns | Process and apparatus for treating moist radioactive wastes |
GB2163894A (en) * | 1984-08-16 | 1986-03-05 | Nuklear Service Gmbh Gns | Preparing radioactive waste solids and evaporator concentrates for final storage in permanent storage containers |
DE3432103A1 (de) * | 1984-08-31 | 1986-03-13 | Kraftwerk Union AG, 4330 Mülheim | Verfahren zum volumenreduzierung von radioaktiv beladenen fluessigkeiten und rippenkoerper zur verwendung dabei |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1088624B (de) * | 1959-06-27 | 1960-09-08 | Ver Kesselwerke Ag | Verfahren und Vorrichtung zum Entfernen von radioaktiven Verunreinigungen aus Fluessigkeiten, insbesondere aus Wasser, durch Eindampfen |
DE3029147A1 (de) * | 1980-07-31 | 1982-02-25 | Kraftwerk Union AG, 4330 Mülheim | Verfahren und anlage zur behandlung radioaktiver rueckstaende aus borathaltigen abwaessern |
-
1988
- 1988-08-17 DE DE19883827897 patent/DE3827897A1/de active Granted
-
1989
- 1989-08-03 EP EP19890114316 patent/EP0355514A3/fr not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1614497A1 (de) * | 1967-04-12 | 1970-08-20 | Siemens Ag | Verfahren zur Konzentrierung radioaktiver Abfaelle |
FR2307342A1 (fr) * | 1975-04-11 | 1976-11-05 | Licentia Gmbh | Procede de traitement de concentres radioactifs |
GB2113902A (en) * | 1982-01-08 | 1983-08-10 | Nuklear Service Gmbh Gns | Process and apparatus for treating moist radioactive wastes |
GB2163894A (en) * | 1984-08-16 | 1986-03-05 | Nuklear Service Gmbh Gns | Preparing radioactive waste solids and evaporator concentrates for final storage in permanent storage containers |
DE3432103A1 (de) * | 1984-08-31 | 1986-03-13 | Kraftwerk Union AG, 4330 Mülheim | Verfahren zum volumenreduzierung von radioaktiv beladenen fluessigkeiten und rippenkoerper zur verwendung dabei |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995026556A1 (fr) * | 1994-03-25 | 1995-10-05 | British Nuclear Fuels Plc | Sechage de dechets radioactifs ou toxiques humides ou d'autres dechets humides dangereux |
ES2184540A1 (es) * | 1999-10-26 | 2003-04-01 | Equipos Nucleares Sa | Procedimiento para tratamiento de residuos liquidos radiactivos y su almacenamiento posterior. |
EP2733704A3 (fr) * | 2012-11-16 | 2016-06-29 | Hartmut Grunau | Récipient de stockage final et procédé de séchage d'objets contaminés dans un récipient de stockage final ainsi que procédé de fabrication de celui-ci |
EP3203482A1 (fr) * | 2012-11-16 | 2017-08-09 | Hartmut Grunau | Récipient de stockage ultime et procédé de séchage d'objets contaminés dans un récipient de stockage ultime |
Also Published As
Publication number | Publication date |
---|---|
EP0355514A3 (fr) | 1991-12-27 |
DE3827897A1 (de) | 1990-03-22 |
DE3827897C2 (fr) | 1992-07-30 |
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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17P | Request for examination filed |
Effective date: 19890803 |
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STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
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18W | Application withdrawn |
Withdrawal date: 19920324 |
|
R18W | Application withdrawn (corrected) |
Effective date: 19920324 |