105 discrepancy assessed Fed+ FeOx + FeOyNat +. FeCz ⦠⢠Na4FeO3. =? (FeO)(Na2O)2). ⢠thermodynamic data (Fe â Na - C â O) system. â Diffusivities (all ...
GROUPEMENT DE RECHERCHE CEA - CNRS - EDF - AREVA NP
3rd International Topical Seminar JAEA / CEA on Coolant and Innovative Reactor Technologies
Sodium corrosion studies in support of SFR : state of the art CEA / DEN / Saclay DPC / SCCME : Behaviour of materials in nuclear, industrial, natural and biological environments, from the understanding of elementary processes up to the development of predictive integrated models for industrial applications, permanents staff : >60, PhD >15 , Lab. > 4000 m² LECNA : J-L. Courouau, V. Lorentz, F. Balbaud
DEN-DPC-SCCME - LECNA
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1
Plan
1- Introduction 2- Short literature review 3- R&D programme 4- Testing device design 5- Prospect and others issues
DEN-DPC-SCCME - LECNA
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2
Introduction
1
• Excellent compatibility of steel with pure liquid sodium, specifically the austenitic steels used in the reactors built up to today in their given operating conditions • Context : new needs for the 2020 SFR prototype or for the SFR (materials // operating conditions // alternative coolant for secondary circuit or for energy conversion systems) Components
Materials
Normal operating conditions
Service life time
Transient conditions
Core
Fuel clad: A 15/15-25 Ti, F/M 9-13-18Cr ODS S. Assembly : F/M 9-12 Cr
thin thick
370-550°C Hot peak : 650°C 8-12 m/s [O] < 5 ppm
4 y and more
T transient : 850°C(boiling) during a few hours max. number of event to be determined Chemistry transient : [O] = 15 ppm / 100 h
Fixed primary structures
A 316 LN
thick
400 - 450°C A few m/s [O] < 5 ppm
60 years
T transient : 850°C(boiling) during a few hours max. number of event to be determined Chemistry transient : [O] = 15 ppm / 100 h
Hot primary structures and components (pump, heat ex)
A 316LN F/M 9-12 Cr
thin thick
400 -550°C A few m/s [O] < 5 ppm
10y ? in case of Ni transfer via Na • Needs : – Not critical for use at T> 316L
Baqué_1981
EM12 - 640°C,
2 m/s, 1 ppm O - 8800 h • Restructuration in large grains • Weight loss 2011)
Lab. Scale experiment: Mechanisms & Modeling :
Specific testing device required
Well adapted for parametric testing over extended operating conditions including transients Saclay
Temperature - time - Re - [O]
Pilot scale experiment : validation Coupling effects
Cadarache
DEN-DPC-SCCME - LECNA
2009
T – t - Re - [O] close to normal operating conditions Reproduction or diffusion prohibited without CEA authorization
2012
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Corrosion testing device
1
CORRONa (CORROsion Na)
Principle: thermal well with rotating cylinders and sodium mini-loop for chemistry control
- thermal well in gloves box for T control - inert crucible in contact with Na at high T to avoid any contamination - Na recirculation (mini loop) for chemistry control - rotating cylinders to control hydrodynamics
A A
?
- make sodium fire a negligible risk (double confinement, leaks detection, very low volume) - thermal control (cooling of the flange)
CEA Saclay - Bat 458 pièce 3
DEN-DPC-SCCME - LECNA
A
Moteur
?
Moteur
Recirculation
Recirculation
Cylindre éprouvette
Constraints :
A
LIBS
1ière barrière
Purificati Purification on
Purificati on Purification Cylindre éprouvette
2ième barrière
2 complementarily testing devices Na = 3.1 kg each Operating conditions: T = 500 - 625°C (designed for 750 °C) v = 500 - 10 000 tr/min (Re) [O] = 0,7 à 38 ppm Mini-loop : 1 l/h, 110-250°C with cold trap (= reactor circuits) Crucible : Molybdenum (MLR – 0.7% La2O3) Well : Nickel base alloy 625 Reproduction or diffusion prohibited without CEA authorization
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Corrosion testing device
2 Laser
Laser LIBS (hublots) Moteur Brushless Moteur des cylindres tournants
Dé tection entré air (Zirox) Mini piège froid : 1 dl
Accouplement magnétique
Bride d’accostage puits Plancher BàG
Argon
Mini pompe Electro magnétique 1 l/h
Mini boucle de recirculation Joints
Boites à huile (thermocryostat)
Plaques de coupure thermiques Isolant céramique
Mécanisme tournant
Bac de rétention + Détection de fuite Na
Puits Creuset en Mo Coupons Na Cylindres Four Dé tection de fuite Na
Air
Accostage
Calorifuge
Creuset Na et internes
DEN-DPC-SCCME - LECNA
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12
Corrosion testing device
3
Change of cylinder :
DEN-DPC-SCCME - LECNA
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13
Corrosion testing device
4
• Cooling fluid circuits Zone de refroidissement du palier
Traversée étanche sur Kf 40
Zone interne
Zone de refroidissement du couvercle Bride de jonction Bride d’accostage
Zone externe C2 ? C1 ?
R2 ?
R1 ?
BàG ?
Zone de refroidissement de la bride
C2 ?
Zone de refroidissement du pot
C1 ? R1 ?
Vanne réglante
R2 ?
bypasse
BàG ? XT750 XT150
DEN-DPC-SCCME - LECNA
2 thermocryostats
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Corrosion testing device
5
• Sodium mini loop for chemistry control Vannes de la purge Préchauffages
Lignes de siphonage
h’ = 100 h = 100
Lignes de Gaz Piège froid Raccords swagelok ou SPG S
PEM
Bac de rétention +Détection de fuite Na par collier
CT
EM P
PEM
• Depressurization line (sodium/oil reaction) Disques de rupture Filtre à vapeur
Filtre à vapeur
Vue de haut
Clapet anti retour
DEN-DPC-SCCME - LECNA
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Prospect and others issues • CORRONA : 1 st test on well ? planned for October 2009 (625°C – 1000h - Re=0 - low [O]) • Materials program (priorities) : – CEA ODS steels (3 nuances) : never tested in sodium, mechanism, modeling – Fe-9Cr : little tested in Na, mechanism, modeling – Austenitic : model strengthening • Collaborations /other development support / support from – GD-MS measurement (M. Tabarant) for sodium sampling analysis - Saclay DPC /LRSI – LIBS (D. L’hermite, JB. Sirven) for on line chemistry monitoring - Saclay DPC /LRSI – Oxygen electrochemical measurement (V. Ghetta, C. Steil, J. Fouletier) - LEPMI/LPSC Grenoble – Electrochemical similitude, CFD modeling, EMP (A. Alemany SIMAP ) (V. Botton, C. Dumont) INSA Lyon – Mechanical properties with liquid metal interaction by Small punch test - Université de Lille (I. Serre, J-B. Vogt) – Mechanical properties with liquid metal interaction – ECP (T. Auger) • Others issues : – Hot concentrated acid corrosion for waste processing – Fissions products corrosion (internal fuel clad corrosion) – Water oxidation at high temperature for the steam generator component – NaOH corrosion (aqueous, concentrated, hot) (stress corrosion cracking) – Corrosion by other medias (Pb-Bi, scCO2) – Hydrogen et materials (embrittlement, tritium) – Water corrosion during storage before processing – Other kind of corrosion
DEN-DPC-SCCME - LECNA
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16