Qualification of the system code AC² (submodule ATHLET) for the safety assessment of passive residual heat removal systems

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Qualification of the system code AC² (submodule ATHLET) for the safety assessment of passive residual heat removal systems Daniel von der Cron, Sebastian Buchholz, Andreas Schaffrath Gesellschaft für Anlagen- und Reaktorsicherheit (GRS) ggmbh Daniel.vonderCron@grs.de International Conference on Topical Issues in Nuclear Installation Safety: Safety Demonstration of Advanced Water Cooled Nuclear Power Plants Vienna 6 9 June 2017

Outline AC² and ATHLET description Passive Residual Heat Removal Systems: The KERENA Emergency Condenser NOKO facility description ATHLET simulations of the NOKO facility: Recent and current activities Conclusion & Outlook 2

AC² Thermal-hydraulic link in the GRS nuclear simulation chain presentation The Nuclear Simulation Chain of GRS Covers operational states, incidents, accidents, severe accidents Comprises the GRS modules: ATHLET primary and secondary system; no core degradation ATHLET-CD extension for core degradation COCOSYS containment phenomena ATLAS post-processing tool for all modules 3

ATHLET Analysis of the THermal-hydraulics of LEaks and Transients System code for comprehensive and realistic analyses of the thermal-hydraulic behavior of the coolant system of a nuclear power plant Substantial validation basis (LOCAs, transients, ) Original 1D code (2D/3D conservation equations available & under development) Finite volume approach on staggered grid Coupling with CFD and neutronics codes possible Focus is on the simulation of physical phenomena, not of special components (black boxes) 4

Passive Residual Heat Removal (PRHR) Systems Passive systems (cf. IAEA-TECDOC-1624): Can contribute to simplification and potentially improve economics Increase the reliability of the performance of essential safety functions PRHR: Removal of residual heat even in the case plant power is lost Examples: AP600/1000: PRHR-HX VVER-1200 (AES-2006): Steam Generator PHRS KERENA: Emergency Condenser (EC) Challenge for ATHLET: Operation usually starts on its own (i.e. no activation signal) Driving forces of operation may vary during the course of a transient dependent on the boundary conditions Conditions may be beyond the range of validity of implemented correlations 5

The KERENA Emergency Condenser (EC) SWR600/1000 (Siemens AG): 4 ECs Maximum heat removal capacity: 63 MW per EC KERENA (AREVA) as successor of SWR600/1000: EC principle is the same, details differ (e.g. 61 condenser tubes instead of 104) Graphic taken from Krepper /KRE 07/ 6

The KERENA Emergency Condenser (EC) Characteristics & phenomena: Slightly inclined horizontal pipes Condensation inside the tubes (depending on local flow pattern) Convective boiling outside Free convection in water pool Graphic taken from Schaffrath /SAN 16/ Test facilities simulated with ATHLET: NOKO (FZ Jülich; single component experiments) TOPFLOW (HZDR; single component experiments) INKA (AREVA; integral tests) 7

The NOKO test facility Thermo hydraulic test rig, scale 1:13 resp. 1:26 (original size condenser tubes; scaled by the number of tubes used) Max. power of electrical heater: 4 MW Experiments carried out under quasistationary conditions Steam supply Pressure vessel Condenser tube bundle Nodalization scheme in ATHLET (condenser vessel only sketched) Condenser vessel (heat sink) Condensate drainage 8

EC power [MW] ATHLET 3.0 simulations of the NOKO facility 4 3 2 Experiment ATHLET 3.0 1 0 0 50 100 150 200 (T Sat,prim - T Sat,sec ) [K] 9

Code modifications ATHLET 3.0 ATHLET 3.1 Secondary side (subcooled/saturated nucleate boiling): Suppression factor in Chen-equation for convective boiling is set to 1.0 for flow outside of horizontal tubes htc CB = S htc PB + F htc FC Thom-equation for estimation of ΔT = T Wall T Sat was replaced by the actual temperature difference of the last time step Primary side (condensation in horizontal pipes): Laminar: Jaster & Kosky modification of Chato-equation Turbulent: Model of Dobson & Chato (based on primitive flow patterns) Convective boiling Pool boiling Forced convection 10

EC power [MW] ATHLET 3.1 simulations of the NOKO facility 4 3 2 Experiment ATHLET 3.0 ATHLET 3.1 1 0 0 50 100 150 200 (T Sat,prim - T Sat,sec ) [K] 11

Current work: Joint project PANAS General information: Funded by BMBF Consortium partners: TUD-WKET, THD, AREVA GmbH, HZDR GRS is a subcontractor of TUD-WKET Project period: 07/2015 12/2018 Project objectives: Investigation of passive decay heat removal systems Experimental analyses Modeling and validation for system codes and CFD codes GRS subtask: Validation and if necessary improvement of condensation and evaporation heat transfer models for ATHLET 12

PANAS: Data used for validation Data used for validation from COSMEA experiments performed at HZDR Graphic taken from Szijártó /SZI 15/ Single effect test stand Focus on flow patterns and condensation processes Secondary side cooled by convection Instrumentation: i.a. thermocouples and X-ray tomography system 13

PANAS: ATHLET modifications made so far Implementation of condensation heat transfer model of Thome et al. Flow pattern map Example (R-12 at 40 C) acc. to El Hajal et al. /HAJ 03/ Heat transfer rather mechanistic modelling htc ges = f (htc conv, htc cond, θ strat ) condensate film condensate pool (axial flow direction) 14

ሶ ሶ PANAS: ATHLET modifications made so far Implementation of condensation heat transfer model KONWAR /SCH 96/ Flow pattern map Heat transfer acc. to Tandon et al. /TAN 82/ Combination of (semi-)empirical models for different flow regimes j x m D = A g d ρ v ρ l ρ 0.5 v 15

EC power [MW] ATHLET 3.1 + THOME simulations of the NOKO facility 4 3 Experiment 2 ATHLET 3.0 ATHLET 3.1 THOME KONWAR 1 0 0 50 100 150 200 (T Sat,prim - T Sat,sec ) [K] 16

EC power [MW] ATHLET 3.1 + KONWAR simulations of the NOKO facility 4 3 Experiment 2 ATHLET 3.0 ATHLET 3.1 THOME KONWAR 1 0 0 50 100 150 200 (T Sat,prim - T Sat,sec ) [K] 17

Conclusions & Outlook Conclusion ATHLET 3.0 3.1: significant improvement of heat transfer Implementation of Thome et al. and KONWAR: smaller improvements Next steps Validation of implemented models by simulation of COSMEA experiments If it proves necessary: modification of heat transfer correlations at tube bundle shell side Moreover: Joint project EASY (03/2015 02/2018; focused on integral tests at INKA) 18

Acknowledgements The project PANAS (reference number 02NUK041), where GRS is a subcontractor of Technische Universität Dresden, Chair of Hydrogen and Nuclear Energy, is funded by the German Federal Ministry of Education and Research (BMBF). The code modifications from ATHLET version 3.0 to version 3.1 were funded by the German Federal Ministry of Economic Affairs and Energy (BMWi) within the project RS1507. 19

References /HAJ 03/ J. El Hajal, J. R. Thome, A. Cavallini. Condensation in horizontal tubes part 1: two-phase flow pattern map. International Journal of Heat and Mass Transfer, vol. 46, no. 18, pp. 3349-3363. 2003 /KRE 07/ E. Krepper. Experimental and numerical investigations of an emergency condenser. 4th NC IAEA Research Coordination Meeting. Vienna, Sept. 10th-13th 2007 /SAN 96/ A. Schaffrath. Experimentelle und analytische Untersuchungen zur Wirksamkeit des Notkondensators des SWR600/1000, Jül-3326, Forschungszentrum Jülich, 1996 /SAN 16/ A. Schaffrath, A. Krüssenberg, S. Buchholz. International Developments, Safety Issues and Modelling Gaps of SMRs, 11th International Topical Meeting on Nuclear Reactor Thermal-Hydraulics, Operation and Safety (NUTHOS-11), 9.-13. October 2016, Gyeongju (Korea) /SZI 15/ R. Szijártó. Condensation of steam in horizontal pipes: model development and validation. Diss.-No. ETH 22550. ETH Zurich, 2015 /TAN 82/ T.N. Tandon, H.K. Varma, C.P. Gupta. A New Flow Regimes Map for Condensation Inside Horizontal Tubes. Journal of Heat Transfer, vol. 104, pp. 763-768. 1982 20