INSTAB Couplings and instabilities in reactor systems Markku Puustinen, Jani Laine, Antti Räsänen, Lauri Pyy, Eetu Kotro, Vesa Tanskanen, Elina Hujala Lappeenranta University of Technology SAFIR2018 Interim Seminar, March 23-24, 2017, Espoo INSTAB – Motivation Condensation pool is an in-containment heat sink in BWRs Steam discharges are received from Upper dry well safety/relief valves and blowdown pipes Water discharge from containment spray and Residual Heat Removal (RHR) return lines Blowdown pipes Thermal stratification of the condensation pool limits the volume of water absorbing heat • Full capacity of the pool not used containment overpressure risk Wet well Lower dry well The INSTAB project studies the stability of stratification and mixing mechanisms in pool SAFIR2018 Interim Seminar 3 INSTAB – Enhancement of safety Earlier LUT POOLEX and PPOOLEX projects have addressed the blowdown pipe performance • direct contact condensation (DCC) leads to instability – chugging – which causes large dynamic mechanical loads INSTAB focus in 2015-2016 has been on • modelling of stratification and mixing in relation to operation of Safety/Relief Valve (SRV) spargers and Residual Heat Removal (RHR) nozzles • supporting the development of the Effective Heat Source (EHS) and Effective Momentum Source (EMS) models, originally developed by KTH • already successfully developed for blowdown pipes • supporting CFD code modelling of direct contact condensation situations at LUT and VTT SAFIR2018 Interim Seminar 4 INSTAB – PPOOLEX test facility Height 7.45 m, diameter 2.4 m, volume 31 m3 • Max pressure 0.5 MPa • Steam from the nearby PACTEL facility (1 MW) Pressure, differential pressure, temperature, flow, strain and relative humidity measurements • kHz range measurements and data acquisition Triple high speed camera and stereo Particle Imaging Velocimetry (PIV) systems SAFIR2018 Interim Seminar 5 INSTAB – Sparger tests: stratification erodes away Pool water above sparger “mouth” warms up ~uniformly Simultaneously, the thermocline moves downwards No chugging, condensation of small steam jets Complete mixing of the water pool through an erosion process was achieved in the end SAFIR2018 Interim Seminar 6 INSTAB – Erosion is due to large-scale turbulence Flow field in the vicinity of the thermocline can be resolved by PIV Large eddies exist around the elevation of the thermocline SAFIR2018 Interim Seminar 7 INSTAB – Direct Contact Condensation model development with NEPTUNE_CFD CFD modelling of DCC requires that the interfacial area density between the liquid and vapour phases is resolved • either by using a very dense computational grid, or • by applying a special interfacial instability model Interfacial area density has been modelled in the NEPTUNE_CFD code with the help of a plausible and simple solution of RayleighTaylor instability (RTI), originally introduced by Pellegrini et al. • The model seems to perform qualitatively well enough Simulations of a plexiglass blowdown pipe case in PPOOLEX have been done in order to further investigate the effect of the RTI model on calculation results of DCC SAFIR2018 Interim Seminar 8 INSTAB – Highlights from CFD calculations The condensation rate is higher and the shapes of fully expanded bubbles are different in the case with the Rayleigh-Taylor instability model (left) compared to the case without it (right) • In general the RTI model seems to give results closer to reality with a low resolution mesh SAFIR2018 Interim Seminar 9 INSTAB – Pressure data interpretation Frequency in FFT [Hz] Possible source of frequency 0.5–3.5 chugging frequency 11–12 vessel 41–45 natural frequency of the bubble 80–83 vessel 150 vessel 250–300 bubble/blowdown pipe SAFIR2018 Interim Seminar Pressure data from earlier PPOOLEX tests were fast Fourier transformed (FFT) and compared to the bubble oscillation results of the NEPTUNE_CFD simulations It is possible to identify from the test data frequencies caused by the blowdown pipe, test vessel and bubbles themselves This helps DCC modellers focus on reproducing bubble condensation correctly 10 INSTAB – Highlights from RHR nozzle tests To obtain data for extending the EMS and EHS models to RHR system nozzles a series of tests was done in PPOOLEX The effects of nozzle orientation, T in the pool, injection water temperature and injection water mass flow rate on mixing efficiency were studied • Thermally stratified condition was created by injecting steam into the pool water via the sparger pipe • Two regions with clearly different water temperatures and a narrow thermocline region between them developed in the pool Compete mixing was achieved with the horizontal orientation of the RHR nozzle SAFIR2018 Interim Seminar 11 INSTAB – Highlights from RHR nozzle tests With the vertical orientation of the RHR nozzle mixing was otherwise successful but incomplete above the nozzle elevation SAFIR2018 Interim Seminar 12 INSTAB – CONCLUSIONS INSTAB tests have generated a large database on suppression pool phenomena • Data on stability of pool stratification and efficiency of pool as heat sink • Strong contribution to the development of the EMS and EHS models for blowdown pipes, SRV spargers and RHR nozzles DCC modelling in CFD (Fluent, NEPTUNE_CFD, OpenFOAM) evaluated on the basis of the PPOOLEX tests • Rayleigh-Taylor instability modelling for the interface is very promising Closures for the EMS/EHS models: in 2017-2018, • PPOOLEX spray tests will be conducted • separate effect tests, where momentum induced by steam injection through a sparger is measured directly SAFIR2018 Interim Seminar 13 Thank you for your attention SAFIR2018 Interim Seminar 14 INSTAB – Plans for steam jet testing In 2017, a separate effect test facility will be constructed and momentum created by steam discharge through sparger holes will be measured directly in order to provide closures for the EMS model development work for spargers Flexible junction Once the EMS and EHS models have been validated for spargers, they can be implemented also to other codes than GOTHIC Force measurements Pipe fixed and allowed to rotate around this point Steam injection ~300 ~500 Open ceiling ~1000 SAFIR2018 Interim Seminar 15
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