EP0803127A1 - Verfahren zur reduzierung von radioaktiven abfällen, wie insbesondere öl oder lösungsmittel und vorrichtung für dieses verfahren - Google Patents

Verfahren zur reduzierung von radioaktiven abfällen, wie insbesondere öl oder lösungsmittel und vorrichtung für dieses verfahren

Info

Publication number
EP0803127A1
EP0803127A1 EP95907032A EP95907032A EP0803127A1 EP 0803127 A1 EP0803127 A1 EP 0803127A1 EP 95907032 A EP95907032 A EP 95907032A EP 95907032 A EP95907032 A EP 95907032A EP 0803127 A1 EP0803127 A1 EP 0803127A1
Authority
EP
European Patent Office
Prior art keywords
waste
electrostatic
filtration
contaminated
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
Application number
EP95907032A
Other languages
English (en)
French (fr)
Other versions
EP0803127B1 (de
Inventor
Adolphe Weber
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bernatom Sarl
Original Assignee
Bernatom Sarl
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bernatom Sarl filed Critical Bernatom Sarl
Publication of EP0803127A1 publication Critical patent/EP0803127A1/de
Application granted granted Critical
Publication of EP0803127B1 publication Critical patent/EP0803127B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • G21F9/06Processing
    • G21F9/10Processing by flocculation

Definitions

  • the present invention relates to the field of treatment of radioactive waste, in particular of oils and solvents, in particular in nuclear power stations and in military study centers, and relates to a process for reducing waste suitable for this purpose. .
  • the invention also relates to a device for implementing this method.
  • Contaminated oil is understood to mean an oil containing radioactive substances.
  • the decontamination processes of known contaminated oils and solvents are centrifugation, decantation, filtration on rare earths and bacterial destruction.
  • DE-A-3 522 126 discloses a process for centrifuging radioactive effluents and drying solid residues.
  • JP-A-63 204 198 describes a process for centrifuging and filtering radioactive effluents containing an oily part.
  • Also known from WO-A-89 08316 is a process for treating weakly radioactive effluents by preheating eliminating volatile solvents, then by special centrifugation followed by filtration.
  • the present invention aims to overcome these drawbacks. Its object is in fact a process for the reduction of radioactive waste, in particular of oils and solvents, in particular in nuclear power stations and in military study centers, characterized in that it consists essentially in pouring said waste in a tank, in which it is subjected to continuous agitation, to preheat it, to carry out a chemical precipitation treatment, to pass the mixture through a centrifuge, to carry out electrostatic or conventional filtration and then to control the level of radioactivity, the treatment being continued continuously until the desired level of decontamination is reached.
  • the invention also relates to a device for implementing this process, essentially consisting of a contaminated waste tank connected, by means of supply and return pipes and by a circulation pump, to an element filter, characterized in that it is further provided, between the contaminated waste tank and the filter element, with a centrifuge intended to separate the water possibly contained in the waste and to carry out the separation of large contaminated particles, so as to limit the consumption of filter elements, in that the tank is provided with a mixer and a heating means and in that the filter element consists of at least one collector electrostatic or a conventional filter, all of the elements being controlled and controlled by means of a control panel.
  • FIG. 1 is a side elevational view in section of a device for implementing the method according to the invention
  • FIG. 2 is a partial plan view of the device
  • Figure 3 is a partial schematic view in side elevation and in section showing the operation of an electrostatic collector.
  • the process for reducing radioactive waste essentially consists in pouring said waste into a tank 1, in which they are subjected to continuous stirring by means of a mixer 8, to preheat these by means of a heating means 6, to carry out a chemical precipitation treatment, to pass the mixture through a centrifuge 2, by through supply and return lines 4 and a pump 5, to carry out electrostatic or conventional filtration in a filtration element 7, and then to control the rate of radioactivity, all of the operations being controlled and controlled by means of a control panel 9, the treatment being continued continuously until the desired decontamination rate is reached, by return of the treated waste by means of a co Return line 4 to the tank 1.
  • the preheating of the waste by the heating means 6 is advantageously carried out at a temperature between 15 ° C and 80 ° C.
  • This process is implemented by means of a device essentially consisting of a reservoir 1 of contaminated waste connected, by means of supply and return lines 4 and by a circulation pump 5, to a filtration element 7, this device being characterized in that it is further provided, between the contaminated waste tank 1 and the filter element 7, with a centrifuge 2 intended to separate the water possibly contained in the waste and to carry out the separation of large contaminated particles, in that the tank 1 is provided with a mixer 8 and a heating means 6 and in that the filtration element 7 is constituted by at least one electrostatic collector or a conventional filter, all of these elements being controlled and controlled by means of a control panel 9.
  • the filtration element 7 is constituted by one or more electrostatic collectors or by conventional filters, the waste supply of which is carried out, at their lower part, by means of the circulation pump 5, this or these electrostatic collectors being connected in the upper part to the return pipe 4, as shown in FIG. 1 of the accompanying drawings, or the conventional filters being connected in the lower part to the return pipe 4, their supply being done from above.
  • This variant embodiment is not shown in the accompanying drawings.
  • the conventional electrostatic collector (s) or filters forming the filtration element 7 are preferably provided with removable and interchangeable filter elements made of paper. Thus, by periodically changing the paper filter elements, the contamination accumulated on them can be eliminated in compliance with the regulations in force.
  • the heating means 6, the thermostat of which makes it possible to regulate the temperature between 15 ° C and 80 ° C, is intended to maintain a low and constant viscosity of the waste to be treated throughout the duration of the treatment operation and therefore to promote good circulation of this waste in the centrifuge 2 and in the filtration means 7.
  • the device is completed by a centrifuge 2 mounted in deflection on the supply line 3 and the outlet of contaminated waste is connected to the tank 1.
  • a centrifuge is intended to remove water so that its rate in the waste contaminated is less than 500 ppm. A rate higher than this value would change the insulating characteristics of the oil and interfere with electrostatic filtration.
  • FIG. 3 of the accompanying drawings shows a principle of electrostatic filtration as implemented by the invention. It appears from this figure that the particles circulating in an electric field between a positive electrode and a negative electrode are attracted, according to their negative or positive charge, by the two electrodes.
  • the charged particles are attracted, according to their polarity, against the corresponding filtering face of the plywood elements 10 and are there retained, so that the contaminated waste is discharged during its passage through the collectors, in porous material such as paper, for example according to the vertical arrows shown in the lower part of FIG. 3, of all or part of the charged particles.
  • the circulation of contaminated waste is maintained until a contamination threshold of a value of the same order as that of natural radioactivity is reached, or even lower.
  • the decontaminated oils obtained can therefore be treated in existing recycling facilities or for the destruction of used oils, for example by incineration in a cement plant.
  • the active particles generally contained in radioactive waste are essentially particles of the type 54Mn, 58Co, 59Fe, 60co, 65zn, 134Cs, 137Cs, and their treatment by application of the process according to the invention by means of the device described above allows a considerable reduction in the volume and weight of the waste in a ratio that can vary between 1 to 1000 and 1 to 3000.
  • contamination is mainly due to uranium and other actinides.
  • the process according to the invention makes it possible to trap all of these elements.
  • the purpose of the chemical reduction treatment in the tank 1 is to change the metal ions into metal elements, which are then retained in the electrostatic collector of the filtration element 7. For example, a cobalt ion ( Co ++) will become (CO °) according to the principle (M ++ + 2e -> M °).
  • the method consists in adding to the effluent, beforehand, a so-called entraining salt. The ionic valence of the element will determine the type of trainer to use.
  • oils from nuclear power plants are advantageously reduced by using boron salt, such as, in particular, sodium borhydride, added in an amount of 0.001% to 0.2% by weight. It is, however, also possible to use other reducers.
  • boron salt such as, in particular, sodium borhydride
  • the decontamination of an oil originating from the primary pump of a nuclear power station and having a viscosity of 40 Cst and an activity of 180 Bq / 1 at a value lower than 4 Bq / 1 has been performed as follows:
  • NaBH4 sodium borhydride
  • the method and the device in accordance with the invention allow decontamination by using only electrical energy which simultaneously warms up and circulates the waste to be decontaminated and fixes the active particles in the filtration element.
  • Such a treatment process can be carried out semi-automatically, human intervention being able to be limited to the preliminary chemical treatment and to the replacement of filter papers.

Landscapes

  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
EP95907032A 1995-01-12 1995-01-12 Verfahren zur reduktion von radioaktiven abfällen wie insbesondere ölen oder lösungsmitteln und anwendung dieses verfahrens zur behandlung eines aktivierten öls Expired - Lifetime EP0803127B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/FR1995/000041 WO1996021933A1 (fr) 1995-01-12 1995-01-12 Procede de reduction de dechets radio-actifs, notamment d'huiles et de solvants et dispositif pour la mise en ×uvre de ce procede

Publications (2)

Publication Number Publication Date
EP0803127A1 true EP0803127A1 (de) 1997-10-29
EP0803127B1 EP0803127B1 (de) 1998-12-23

Family

ID=9474860

Family Applications (1)

Application Number Title Priority Date Filing Date
EP95907032A Expired - Lifetime EP0803127B1 (de) 1995-01-12 1995-01-12 Verfahren zur reduktion von radioaktiven abfällen wie insbesondere ölen oder lösungsmitteln und anwendung dieses verfahrens zur behandlung eines aktivierten öls

Country Status (5)

Country Link
US (1) US5875406A (de)
EP (1) EP0803127B1 (de)
DE (1) DE69506916T2 (de)
ES (1) ES2128711T3 (de)
WO (1) WO1996021933A1 (de)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1754232B1 (de) * 2004-05-30 2013-06-26 Pebble Bed Modular Reactor (Proprietary) Limited Verfahren zur behandlung von radioaktivem abfall
DE102011082285A1 (de) * 2011-09-07 2013-03-07 Itn Nanovation Ag Verfahren zur Abtrennung von radioaktiven Nukliden mittels keramischer Filtermembranen
DE102016117703B4 (de) 2016-09-20 2018-04-26 applicsign ag Vorrichtung zur Behandlung von radioaktiv kontaminierten Abwässern
CN109859875A (zh) * 2019-01-16 2019-06-07 中国辐射防护研究院 一种放射性废润滑油的去污解控方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4615794A (en) * 1984-08-20 1986-10-07 Belanger Roger L Method of removing radioactive waste from oil
DE3522126A1 (de) * 1985-06-20 1987-01-02 Kraftwerk Union Ag Einrichtung zur behandlung radioaktiver abwaesser aus kerntechnischen anlagen
US4681705A (en) * 1985-10-15 1987-07-21 Carolina Power & Light Company Decontamination of radioactively contaminated liquids
FR2601182B1 (fr) * 1986-07-07 1992-01-24 Electricite De France Procede pour la decontamination radioactive d'un lubrifiant
DE3644396C1 (de) * 1986-12-24 1988-02-11 Martin Ganter Verfahren zur Dekontamination radioaktiv belasteter Fluessigkeiten
JPH0326999A (ja) * 1989-06-23 1991-02-05 Toshiba Corp 放射性有機物含有廃棄物の処理方法
CN1049179A (zh) * 1989-08-04 1991-02-13 山西省交通科学研究所 废油再生工艺及其生产装置
US5196113A (en) * 1990-02-21 1993-03-23 Southern California Edison Co. Processing mixed waste
US5516969A (en) * 1995-01-23 1996-05-14 Ontario Hydro Waste oil decontamination process

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9621933A1 *

Also Published As

Publication number Publication date
DE69506916T2 (de) 1999-08-05
ES2128711T3 (es) 1999-05-16
DE69506916D1 (de) 1999-02-04
EP0803127B1 (de) 1998-12-23
US5875406A (en) 1999-02-23
WO1996021933A1 (fr) 1996-07-18

Similar Documents

Publication Publication Date Title
EP2253000B1 (de) Verfahren zur dekontaminierung einer radioaktiven flüssigeffluenz mit einem oder mehreren chemischen elementen durch feststoff-flüssigkeit-extraktion mithilfe eines recycling-kreislaufs
CN210030276U (zh) 一种垃圾中转站渗滤液处理装置
JP2007326100A (ja) 汚染された液体及び固体廃棄物から電荷を帯びた化学種を除去するための電気化学的システム及び方法
CN1695834A (zh) 重金属污染土壤的电动力学修复方法
EP1971554A2 (de) Verfahren und system zur behandlung von radioaktivem abwasser
US3236757A (en) Method and apparatus for reclamation of water
EP3160912A1 (de) Verfahren zur behandlung von salzigem wasser
EP0803127B1 (de) Verfahren zur reduktion von radioaktiven abfällen wie insbesondere ölen oder lösungsmitteln und anwendung dieses verfahrens zur behandlung eines aktivierten öls
JPH07974A (ja) 汚染プロセス流からの重金属、放射性汚染要因物の除去方法
AU7519898A (en) Method for removing biomass from a liquid by means of a reactor
CN211896556U (zh) 化学药物研发实验室废水处理设备
DE19902010C2 (de) Verfahren zur Aufbereitung von Asche aus Müllverbrennungsanlagen und von mineralischen Rückständen durch Entsalzung und künstlichen Alterung mittels elektrodynamischer Unter-Wasser-Prozesse und Anlage zur Durchführung des Verfahrens
EP3077131B1 (de) Kombination von reagenzmitteln und verfahren zum entfernen von verunreinigungen aus böden unter verwendung dieser kombination
CN217996939U (zh) 一种带有除渣机构的市政污水治理装置
FR3022538B1 (fr) Procede d'elimination d'un ou plusieurs elements chimiques compris dans une solution aqueuse
CN210097057U (zh) 一种净水处理用前置过滤装置
FR2459067A1 (fr) Installation compacte d'electro-epuration des eaux
CN210163297U (zh) 一种超滤水再生利用装置
AU2010201683A1 (en) Contaminated liquid filtration system vehicle
Markose et al. Leachability of radium from uranium mill tailings
GB2046307A (en) Methods of and apparatus for separating particles from suspensions
JPH09215970A (ja) 陰イオン汚染物の除去における濃度管理方法
Locke Treatment and recycle of high explosive contaminated water
Bridges et al. Cure electrocoagulation demonstration at Rocky Flats Environmental Technology Site
CN110342695A (zh) 一种废切削液的处理方法

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: 19970808

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): BE CH DE ES FR GB LI

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

17Q First examination report despatched

Effective date: 19980520

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

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 ES FR GB LI

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REF Corresponds to:

Ref document number: 69506916

Country of ref document: DE

Date of ref document: 19990204

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 19990325

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19990428

Year of fee payment: 5

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: WERNER FENNER PATENTANWALT

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2128711

Country of ref document: ES

Kind code of ref document: T3

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
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000131

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000131

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20020114

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20020201

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20020205

Year of fee payment: 8

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: 20030112

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20030130

Year of fee payment: 9

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20030131

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: 20030801

GBPC Gb: european patent ceased through non-payment of renewal fee
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040930

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20060215

Year of fee payment: 12

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20070113

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20070113