EP0313843B1 - Procédé pour décontaminer des surfaces - Google Patents
Procédé pour décontaminer des surfaces Download PDFInfo
- Publication number
- EP0313843B1 EP0313843B1 EP88116003A EP88116003A EP0313843B1 EP 0313843 B1 EP0313843 B1 EP 0313843B1 EP 88116003 A EP88116003 A EP 88116003A EP 88116003 A EP88116003 A EP 88116003A EP 0313843 B1 EP0313843 B1 EP 0313843B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- treatment step
- decontamination
- acid
- solution
- surface layers
- 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.)
- Expired - Lifetime
Links
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
-
- 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
- G21F9/001—Decontamination of contaminated objects, apparatus, clothes, food; Preventing contamination thereof
- G21F9/002—Decontamination of the surface of objects with chemical or electrochemical processes
- G21F9/004—Decontamination of the surface of objects with chemical or electrochemical processes of metallic surfaces
Definitions
- the invention relates to a process for the decontamination of surfaces, in particular components of cooling circuits of nuclear reactors, an oxidizing agent being applied in a first treatment step to loosen up the radioactively contaminated surface layers, and the loosened surface layers being removed with the aid of a solvent in a second treatment step.
- EP 0071336 A1 discloses a method for the chemical removal of deposits, in which decontamination is achieved in three steps using permanganate salt. The path taken there apparently avoids the use of chromic acid.
- all known methods for decontaminating the surfaces of components of pressurized water reactors comprise two or more treatment steps, in a first step the insoluble Cr-III oxide being converted into soluble hexavalent chromium in an oxidizing phase and the entire oxide layer being loosened in the process. In a second treatment step, usually after an intermediate rinse, the loosened oxide layer is dissolved and removed in an acidic, regenerative and complex-forming solution.
- the oxidative treatment step are a number of methods in use, such.
- AP alkaline permanganate solution
- NP nitric acid solutions
- Other known processes provide for the use of permanganic acid, hydrogen peroxide, cerium IV salts or other oxidizing agents.
- the decontamination solution used in the first treatment step contains chromic acid (chromium VI oxide) and permanganic acid. Both chromium and manganese are present in all steels commonly used in reactor construction as accompanying or alloying elements. These chemicals are not only inexpensive, but also relatively non-toxic and easy to handle in the concentrations used.
- further substances are added to the decontamination solution used in the first treatment step, which the solvents Make the solution suitable for use in the second treatment step.
- Reducing agents such as oxalic acid, ascorbic acid, formic acid, etc. can be considered as such further substances.
- the reducing agents cause the chromic acid, as well as the permanganic acid and its decomposition products, that is to say also the manganese dioxide, to be converted into soluble chromium III or manganese II salts.
- the permanganic acid can preferably be prepared by passing an aqueous solution of an alkali or alkaline earth permanganate over a cation exchanger, thus forming the free acid which is used as the decontamination agent after the addition of chromic acid.
- Solutions of chromic acid and salts of permanganic acid are also suitable as decontamination agents; however, the additionally introduced cation with the radioactive waste will result in somewhat higher salt loads.
- the pH value and the redox potential of the solution are characteristic of the effectiveness of the decontamination agent.
- the first treatment step can therefore be monitored and controlled by means of these easily detectable measurement variables.
- the reaction of the permanganic acid with constituents of the contaminated oxide layers and the spontaneous decomposition of the permanganic acid produces insoluble manganese dioxide ("manganese dioxide") even at normal room temperatures, which is deposited on the surfaces.
- the discoloration shows the effectiveness of the decontamination solution in a visually verifiable manner. Due to the presence of chromic acid in the decontamination solution, no firmly adhering layers are formed which would then be difficult to remove.
- the surfaces of the cooling circuit components cannot yet be completely freed of radioactive substances by the oxidative first treatment step, which is why a second treatment step is additionally required to remove the surface layers modified by the oxidative treatment.
- the success of the second treatment step can also be checked visually, since the brownish-red-violet colored surface layers disappear from the decontaminated surfaces.
- the effect of the decontamination solution used in the first treatment step can be increased considerably by pumping around, stirring or using ultrasound.
- the same measures can also accelerate the chemical removal of the modified surface layers in the second treatment step.
- the surface layers modified in the first treatment step for example of carbon steels, stainless chromium steels, nickel alloys and other materials customary in reactor construction, can be removed solely by mechanical and / or hydraulic action, for example by means of a high-pressure water jet, in order to ensure that they are flawless To achieve decontamination.
- the solution is then circulated through an ion exchanger and the treated surface is rinsed.
- Samples a) made of ferritic chromium steel were treated at room temperature (290 to 295 K) for 16 hours with a solution of 0.05 mol of chromic and permanganic acids. After an intermediate rinse, a decontamination factor (ratio of measured activity before and after treatment) of 2 was determined. A further treatment at room temperature in an aqueous 0.1 mol solution of oxalic acid under the influence of ultrasound resulted in a decontamination factor of about 20 after 15 minutes and a decontamination factor of over 100 after 6 hours. After the treatment, the decontaminated surfaces of the samples were metallic bright and attacked neither macroscopically nor microscopically recognizable
- Samples c) made of nickel-chromium-iron alloy under the trade name INCONEL 600 were treated at room temperature for 16 hours with a solution of 0.1 mol of chromic acid and 0.004 mol of potassium permanganate. After an intermediate rinse, a decontamination factor of only 1.2 was found. After a further treatment at room temperature with an aqueous solution of 0.1 mol oxalic acid for 6 hours with ultrasound exposure, a decontamination factor of 12 was determined.
- Samples a) made of ferritic chrome steel, samples b) made of austenitic stainless steels and samples c) made of INCOLOY 800 and INCONEL 600 were each in aqueous solutions containing 0.01 to 0.1 mol of chromic acid and 0.001 to 0 for 16 hours at room temperature.
- the samples were then each treated for 6 hours at room temperature in an aqueous solution with 0.1 mol of oxalic acid under the action of ultrasound.
- decontamination factors between 10 and 1000 were measured on all samples.
- Samples a) made of ferritic chromium steel and samples c) made from INCONEL 600 were each treated for 16 hours at room temperature in a solution with 0.1 mol of chromic acid and 0.05 mol of permanganic acid. After a subsequent treatment with a water jet of 2.4 kbar (240 Pa) pressure at a treatment speed of 3.6 m 2 / hour, decontamination factors of about 30 were obtained on samples a) made of ferritic chromium steel and on samples c) made of INCONEL 600 Decontamination factors measured over 100. Extensive follow-up examinations showed that these treatments did not attack the surfaces of the base materials.
- Samples c) from INCONEL 600 were sprayed for 16 hours at room temperature with a solution of 0.05 mol of chromic acid and 0.002 mol of permanganic acid. After a further treatment with a water jet, as in Example 4, decontamination factors between 20 and 80 were determined.
- a paste was prepared from an aqueous solution of 0.4 mol of chromic acid and 0.1 mol of permanganic acid by adding a thickener which is available on the market under the trade name AEROSIL (registered trademark of Degussa).
- AEROSIL registered trademark of Degussa
- the contaminated surfaces of samples a) made of ferritic chrome steel were coated with this paste. After an exposure time of 16 hours, the samples were treated with a water jet, as in Example 4. Decontamination factors between 5 and 15 resulted.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Food Science & Technology (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Chemical Treatment Of Metals (AREA)
Claims (5)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH3846/87A CH673545A5 (fr) | 1987-10-02 | 1987-10-02 | |
CH3846/87 | 1987-10-02 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0313843A1 EP0313843A1 (fr) | 1989-05-03 |
EP0313843B1 true EP0313843B1 (fr) | 1992-07-08 |
EP0313843B2 EP0313843B2 (fr) | 1998-05-13 |
Family
ID=4264738
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP88116003A Expired - Lifetime EP0313843B2 (fr) | 1987-10-02 | 1988-09-28 | Procédé pour décontaminer des surfaces |
Country Status (8)
Country | Link |
---|---|
US (1) | US5093073A (fr) |
EP (1) | EP0313843B2 (fr) |
JP (1) | JPH02503600A (fr) |
KR (1) | KR970011260B1 (fr) |
CH (1) | CH673545A5 (fr) |
DE (1) | DE3872656D1 (fr) |
ES (1) | ES2034088T5 (fr) |
WO (1) | WO1989003113A1 (fr) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4913849A (en) * | 1988-07-07 | 1990-04-03 | Aamir Husain | Process for pretreatment of chromium-rich oxide surfaces prior to decontamination |
DE4232246A1 (de) * | 1992-09-25 | 1994-03-31 | Siemens Ag | Verfahren zur Zerstörung einer organischen Substanz |
US5278743A (en) * | 1992-11-20 | 1994-01-11 | Westinghouse Electric Corp. | Alkaline-permanganate process |
FR2730641B1 (fr) * | 1995-02-20 | 1997-03-14 | Commissariat Energie Atomique | Mousse de decontamination a l'ozone, et procede de decontamination utilisant cette mousse |
US5678232A (en) * | 1995-07-31 | 1997-10-14 | Corpex Technologies, Inc. | Lead decontamination method |
US5591270A (en) * | 1995-07-31 | 1997-01-07 | Corpex Technologies, Inc. | Lead oxide removal method |
CZ233698A3 (cs) * | 1996-02-07 | 1998-12-16 | Buckman Laboratories International, Inc. | Synergicky antimikrobiální prostředky obsahující ionenový polymer a sůl dodecylaminu a způsoby jeho použití |
US5814204A (en) * | 1996-10-11 | 1998-09-29 | Corpex Technologies, Inc. | Electrolytic decontamination processes |
US6183547B1 (en) * | 1998-03-05 | 2001-02-06 | The University Of Notre Dame Du Lac | Environmentally acceptable inhibitor formulations for metal surfaces |
JP2001124891A (ja) * | 1999-07-09 | 2001-05-11 | Hitachi Ltd | 原子力プラント構造物の表面処理方法および原子力プラント |
JP3977963B2 (ja) | 1999-09-09 | 2007-09-19 | 株式会社日立製作所 | 化学除染方法 |
FR2841802B1 (fr) * | 2002-07-08 | 2005-03-04 | Commissariat Energie Atomique | Composition, mousse et procede de decontamination de surfaces |
KR100724710B1 (ko) * | 2002-11-21 | 2007-06-04 | 가부시끼가이샤 도시바 | 방사화 부품의 화학적 오염제거 시스템 및 방법 |
KR20040077390A (ko) * | 2003-02-28 | 2004-09-04 | 김성진 | 핵 방사능 잡 고체, 시멘트, 농축 폐 액 드럼을 천일염수와 천일염으로 절게 하여 고온으로 소각시켜 핵 방사능독을 흔적없이 공중 완전 소각 방법과, 농축 천일염(수)폐액 드럼. |
JP3945780B2 (ja) * | 2004-07-22 | 2007-07-18 | 株式会社日立製作所 | 原子力プラント構成部材の放射性核種の付着抑制方法および成膜装置 |
DE102009047524A1 (de) * | 2009-12-04 | 2011-06-09 | Areva Np Gmbh | Verfahren zur Oberflächen-Dekontamination |
DE102010028457A1 (de) * | 2010-04-30 | 2011-11-03 | Areva Np Gmbh | Verfahren zur Oberflächen-Dekontamination |
EP3033751B1 (fr) * | 2013-08-14 | 2019-10-23 | Framatome GmbH | Procédé pour la réduction de la contamination radioactive d'une surface d'une composante utilisée dans un reacteur nucléair |
DE102013108802A1 (de) * | 2013-08-14 | 2015-02-19 | Areva Gmbh | Verfahren zur Verringerung der radioaktiven Kontamination eines wasserführenden Kreislaufs eines Kernkraftwerks |
US9440847B2 (en) * | 2013-10-03 | 2016-09-13 | POSiFA MICROSYSTEMS, INC. | Single silicon wafer micromachined thermal conduction sensor |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3615817A (en) * | 1969-02-04 | 1971-10-26 | Atomic Energy Commission | Method of decontaminating radioactive metal surfaces |
US4217192A (en) * | 1979-06-11 | 1980-08-12 | The United States Of America As Represented By The United States Department Of Energy | Decontamination of metals using chemical etching |
US4481040A (en) * | 1981-06-17 | 1984-11-06 | Central Electricity Generating Board Of Sudbury House | Process for the chemical dissolution of oxide deposits |
US4522928A (en) * | 1982-10-18 | 1985-06-11 | Exxon Research And Engineering Co. | Removal of metal comtaminants from catalysts using buffered oxalic acid |
SE435329B (sv) * | 1983-02-09 | 1984-09-17 | Studsvik Energiteknik Ab | Dekontaminering av tryckvattenreaktorer |
DE3413868A1 (de) * | 1984-04-12 | 1985-10-17 | Kraftwerk Union AG, 4330 Mülheim | Verfahren zur chemischen dekontamination von metallischen bauteilen von kernreaktoranlagen |
US4913849A (en) * | 1988-07-07 | 1990-04-03 | Aamir Husain | Process for pretreatment of chromium-rich oxide surfaces prior to decontamination |
-
1987
- 1987-10-02 CH CH3846/87A patent/CH673545A5/de not_active IP Right Cessation
-
1988
- 1988-09-28 JP JP88508032A patent/JPH02503600A/ja active Pending
- 1988-09-28 ES ES88116003T patent/ES2034088T5/es not_active Expired - Lifetime
- 1988-09-28 US US07/397,440 patent/US5093073A/en not_active Expired - Fee Related
- 1988-09-28 WO PCT/EP1988/000870 patent/WO1989003113A1/fr unknown
- 1988-09-28 KR KR1019890700977A patent/KR970011260B1/ko active IP Right Grant
- 1988-09-28 DE DE8888116003T patent/DE3872656D1/de not_active Expired - Fee Related
- 1988-09-28 EP EP88116003A patent/EP0313843B2/fr not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP0313843A1 (fr) | 1989-05-03 |
KR890702211A (ko) | 1989-12-23 |
EP0313843B2 (fr) | 1998-05-13 |
CH673545A5 (fr) | 1990-03-15 |
ES2034088T3 (es) | 1993-04-01 |
ES2034088T5 (es) | 1998-10-01 |
US5093073A (en) | 1992-03-03 |
KR970011260B1 (ko) | 1997-07-08 |
DE3872656D1 (de) | 1992-08-13 |
WO1989003113A1 (fr) | 1989-04-06 |
JPH02503600A (ja) | 1990-10-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0313843B1 (fr) | Procédé pour décontaminer des surfaces | |
EP2417606B1 (fr) | Procédé de décontamination de surfaces | |
EP2564394B1 (fr) | Procede pour la decontamination des surfaces | |
EP1955335B1 (fr) | Procede de decontamination d'une surface presentant une couche d'oxyde d'un composant ou d'un systeme d'une centrale nucleaire | |
EP2399262B1 (fr) | Procédé de décontamination de surfaces contaminées par radioactivité | |
CH619807A5 (fr) | ||
DE3013551A1 (de) | Dekontamination von kernreaktoren | |
DE2613351C3 (de) | Verfahren zur chemischen Dekontamination von metallischen Bauteilen von Kernreaktoranlagen | |
DE19818772C2 (de) | Verfahren zum Abbau der Radioaktivität eines Metallteiles | |
CH642475A5 (de) | Verfahren zur chemischen dekontamination von bauteilen. | |
EP2188814B1 (fr) | Procédé de décontamination de surfaces d'installations nucléaires contaminées par des rayons alpha | |
DE3046563A1 (de) | Dekontaminierungsreagens und verfahren zum dekontamiinieren eines kernreaktors oder von teilen davon | |
EP0951582B1 (fr) | Traitement de surface de l'acier ou d'un alliage au nickel et acier ou alliage au nickel ainsi traites | |
EP3033751B1 (fr) | Procédé pour la réduction de la contamination radioactive d'une surface d'une composante utilisée dans un reacteur nucléair | |
EP3607562B1 (fr) | Dosage de zinc pour la decontamination des réacteurs à eau légère | |
DE2511112C3 (de) | Verfahren zum Dekontaminieren von Oberflächen metallischer Werkstoffe | |
DD241617A1 (de) | Verfahren zur entfernung von stabilen oxidschichten auf eisenwerkstoffen | |
DE1256513B (de) | Verfahren zur Entseuchung von mit radioaktiven Korrosionsprodukten verunreinigten Metalloberflaechen | |
DE4310749A1 (en) | Electrochemical decontamination of metal component using strongly alkaline electrolyte liq. - used to remove radioactive oxide layers from PWR and BWR components | |
WO2000028553A2 (fr) | Procede pour eliminer des cations metalliques |
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 DE ES FR GB IT NL SE |
|
17P | Request for examination filed |
Effective date: 19890526 |
|
17Q | First examination report despatched |
Effective date: 19910222 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE ES FR GB IT NL SE |
|
REF | Corresponds to: |
Ref document number: 3872656 Country of ref document: DE Date of ref document: 19920813 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
ET | Fr: translation filed | ||
ITF | It: translation for a ep patent filed |
Owner name: DE DOMINICIS & MAYER S. |
|
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2034088 Country of ref document: ES Kind code of ref document: T3 |
|
26 | Opposition filed |
Opponent name: SIEMENS AKTIENGESELLSCHAFT, BERLIN UND MUENCHEN Effective date: 19930324 |
|
NLR1 | Nl: opposition has been filed with the epo |
Opponent name: SIEMENS AG. |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19940930 Year of fee payment: 7 |
|
EAL | Se: european patent in force in sweden |
Ref document number: 88116003.0 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19960401 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19960401 |
|
APAC | Appeal dossier modified |
Free format text: ORIGINAL CODE: EPIDOS NOAPO |
|
PLAW | Interlocutory decision in opposition |
Free format text: ORIGINAL CODE: EPIDOS IDOP |
|
PUAH | Patent maintained in amended form |
Free format text: ORIGINAL CODE: 0009272 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: PATENT MAINTAINED AS AMENDED |
|
27A | Patent maintained in amended form |
Effective date: 19980513 |
|
AK | Designated contracting states |
Kind code of ref document: B2 Designated state(s): BE DE ES FR GB IT NL SE |
|
ET3 | Fr: translation filed ** decision concerning opposition | ||
GBTA | Gb: translation of amended ep patent filed (gb section 77(6)(b)/1977) | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19980824 Year of fee payment: 11 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: DC2A Kind code of ref document: T5 Effective date: 19980729 |
|
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: 19990928 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19990928 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20010928 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20020903 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20020904 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 20020905 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20021023 Year of fee payment: 15 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030929 Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030929 |
|
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: 20030930 |
|
BERE | Be: lapsed |
Owner name: PAUL *SCHERRER INSTITUT Effective date: 20030930 Owner name: *ABB REAKTOR G.M.B.H. Effective date: 20030930 |
|
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: 20040401 |
|
EUG | Se: european patent has lapsed | ||
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: 20040528 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20030929 |
|
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: 20050928 |
|
APAH | Appeal reference modified |
Free format text: ORIGINAL CODE: EPIDOSCREFNO |