DETAILS OF THE ACCIDENT PROGRESSION IN 1F1

Similar documents
Leaks from Unit-3 PCV and steam release in a large amount

2-Port Seat Valves with Flange, PN 16

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER P: REFERENCE OPERATING CONDITION STUDIES (PCC)

Design DSA Steam-Atomized Desuperheater

Verification and validation of computer codes Exercise

2-Port Seat Valves with Flange, PN 16

Copyright, 2005 GPM Hydraulic Consulting, Inc.

Evaluation of the fraction of Unit-3 vent gas that flowed into Unit-4 reactor building

Ball Float Steam Trap UNA 45 MAX, UNA 46 MAX, UNA 46A MAX PN 40/Class 300 DN 40, 50, 65

Fisher DVI Desuperheater Venturi Inline

English. Introduction. Safety Instructions. All Products. Inspection and Maintenance Schedules. Parts Ordering. Specifications WARNING WARNING

Discharge Relief Valve Operation & Maint.

Unit 24: Applications of Pneumatics and Hydraulics

SCA Series Inverted Bucket Steam Traps

Ball Float Steam Trap UNA 43 PN 16/CL 125/JIS 10K UNA 46 PN 40/CL 150/CL 300/JIS 10K/JIS 20K DN 80, 100, 150, 3", 4", 6"

Air Eliminators and Combination Air Eliminators Strainers

then the work done is, if the force and the displacement are in opposite directions, then the work done is.

Instrumentation systems of BWR

INSTALLATION, OPERATION, AND MAINTENANCE MANUAL WELKER FILTER DRYER

INSTALLATION, OPERATION, AND MAINTENANCE MANUAL WELKER RELIEF VALVE

Waterous Relief Valve

Alkylphosphines. Storage and Handling Recommendations

better measurement Simply a question of SCHMIDT Flow Sensor SS The cost-effective alternative in pressurised systems up to 10 bars.

Hydraulic Reliability & Preventive Maintenance Report

Classical Event Tree Analysis and Dynamic Event Tree Analysis for High Pressure Core Melt Accidents in a German PWR

Fisher DSA Steam-Atomized Desuperheater

TA10A and TA10P Steam Tracing Temperature Control Valves Installation and Maintenance Instructions

FLUID POWER FLUID POWER EQUIPMENT TUTORIAL ACCUMULATORS. This work covers part of outcome 2 of the Edexcel standard module:

Pressure and/or Temperature Pilot Operated Steam Regulators Series 2000

Model 7989T Steel Pipe Squeezer Sch. 40 & Sch. 80. Operations Manual

CAST IRON SAFETY VALVE TYPE 6301

Safety Engineering - Hazard Identification Techniques - M. Jahoda

TEPCO s Safety Assurance Philosophy on Nuclear Power Generation Plants

Jupiter Type 4 Tube Owner s Manual

The Nitrogen Threat. The simple answer to a serious problem. 1. Why nitrogen is a risky threat to our reactors? 2. Current strategies to deal with it.

Effects of Delayed RCP Trip during SBLOCA in PWR

Temperature Controllers

Instruction manual. for. high purity gas pigtails 200 bar / 300 bar

Transferring and Storage

Nuclear safety Lecture 4. The accident of the TMI-2 (1979)

Exercise 2-3. Flow Rate and Velocity EXERCISE OBJECTIVE C C C

BT 800-OX Operating Manual

Safety Shut-off Valve SSV

Pilot Check Valve: Metal Body Type

PRAHER PLC-MP AQUASTAR MANAUL 2009

Engineering & Projects Organization

UBP32 Sealed Balanced Pressure Thermostatic Steam Trap for use with PC_ Pipeline Connectors Installation and Maintenance Instructions

HTR Systems and Components

Safety. April 2018 Supersedes all previous publications 2018 Chevron Phillips Chemical Company LP

Float Operated Level Controllers

Two-port seat valves

Automatic Non-freeze Valve NF6

Flow and check valves Logic valves series 551. Brochure

INTERPLANT STANDARD - STEEL INDUSTRY

TSS21 Sealed Thermostatic Steam Tracer Trap

Dean Pump Self-Priming Chemical Process Pumps

AVS32 Stainless Steel Air Vent for Steam Systems Installation and Maintenance Instructions

Sizing, Selection, and Installation of Pressure-relieving Devices in Refineries

2-Port and 3-Port Seat Valves with Female Thread, PN16

WW-720. Pressure Reducing Control Valve

Accident Management Strategies for Mark I and Mark III BWRs

TEST BENCH SAFETY VALVES ¼ - 5 DN10 DN125

MST21 Stainless Steel Balanced Pressure Thermostatic Steam Trap

Spilt body Flange ball valve. TC-205MFF-PN1640 User Manual English Version. Document No: TC-205MFF-PN1640.Ur-manual. Date: 2007/04/2617. Version: 1.

Valve Inspection & Testing

I T T Pressure Reducing Valve WARNING INSTALLATION, OPERATION, AND MAINTENANCE MANUAL

Mooney * Noise Controller Installation, Operation, and Maintenance Manual

HOW TO NOT MEASURE GAS - ORIFICE. Dee Hummel. Targa Resources

BUTTERFLY VALVES Series 800

INHERENTLY SAFER DESIGN CASE STUDY OF RAPID BLOW DOWN ON OFFSHORE PLATFORM

UIB30 and UIB30H Sealed Inverted Bucket Steam Traps for use with Pipeline Connectors

2 I All-Flo Pump Co.

Fisher Lever Lock Handlever Actuators for POSI SEAL A81 Rotary Valves

Model 4000 Pressure Controller

NORMAL OPERATING PROCEDURES Operating Parameter Information

120 PSI FAST-FILL AIR SOURCE KIT 25% Duty Compressor on 1.5 Gallon Air Tank

WW-720. Pressure Reducing Control Valve

The Discussion of this exercise covers the following points:

Steam Trap BK BK 212-ASME. Original Installation Instructions English

Model PRS-07i. Stainless Steel Low Pressure, In-Line Pressure Regulator (Reducing Valve)

CONTROL VALVE TESTING

1. Preface Important Safety Notes Brief Product Information Product Working Principle Installation Guidelines...

44 (0) E:

VALVCHEQ BACKFLOW PREVENTERS FIGURE RP03

ZZYP TYPE AUTOMATIC PRESSURE REGULATING CONTROLL VALVE

Pressure Independent Control Series

Installation Operation Maintenance

VSR modulating valves with membrane actuator

TESCOM 50-4X Series Safety, Installation & Start-Up Procedures

Restoring Fluid Flow in Tubing Strings

Declaration of Conformity as per Directive 97/23/EC

Operation Manual Guillotine Cutter RC-5

Instruction Manual Model Borehole Pressure Cell

1700ESL Kamvalok Coupler

Fisher Lever-Lock Handlever Actuators for POSI-SEAL A81 Rotary Valves

WATER HEATER THERMAL EXPANSION TANKS Owner s Manual. Safety Instructions Installation Maintenance Warranty. Models: 2-5 Gallon Capacity

Type 92S Pilot-Operated Steam Regulator

200 PSI HIGH-FLOW AIR SOURCE KIT

2 I All-Flo Pump Co.

EASTERN ENERGY SERVICES PTE LTD. 60 Kaki Bukit Place #02-19 Eunos Tech Park Singapore, SG Singapore Telephone: Fax:

Transcription:

DETAILS OF THE ACCIDENT PROGRESSION IN 1F1 EMUG 2019 BRAUN, Matthias Switzerland, 3 rd -5 th April 2019

Not part of the BSAF OECD Benchmark Project Relying exclusively on publically available input data No legal restraints for usage & publication (project and export control) MELCOR 1.8.6 Model for 1F1 Aim is to reproduce 1F1 accident with low (minimum) number of fit parameters Prefer physical models over forced boundary conditions No 1:1 correspondence to measured data desired TEST MODEL not a HOW-TO Handle with care Alternative untested / not recommended modelling techniques Test base for conversion 1.8.6 to 2.x Model & description report freely distributed to MELCOR community (FGF_D02-ARV-01-111-828) Revision B (hardcopy) on EMUG2018 Revision C the MELCOR input model at CSARP/MCAP 2018 Revision D planned end 2019 Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.2

Containment pressure 6 bar-abs at 12 th March 01:00 RCS Leakage before RPV Failure? (I of II) Likely that RPV failure occurs afterward A discharge only via open SRV into the W/W would require > 1500 kg H2 (100% core oxidation) to fill W/W and D/W A steam leak in the D/W compresses N2 + H2 into the W/W requiring ~ 500-800 kg H2 Plant Data published by TEPCO https://www4.tepco.co.jp/en/nu/fukushima-np/index10-e.html Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.3

RCS Leakage before RPV Failure? (II of II) Malfunctioning of RPV water level measurement Containment heat-up via insulated RCS unlikely to be sufficient to cause this malfunctioning RCS leakage before 11 th March 21:30 Dry-out of upper reference line, and very late dry-out of lower sensing line - Leak can not be too large Plant Data published by TEPCO https://www4.tepco.co.jp/en/nu/fukushima-np/index10-e.html Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.4

Modelling of RPV water level measurement Generic 0.5 inch schedule 80 piping No detailed information about piping routing available Limited accuracy!!!! Test Leakage Scenarios via Response of the RPV Level Measurement Complementary to TEPCO 5th Progress Report Attachment 1-6 Gothic simulation of containment https://www7.tepco.co.jp/newsroom/press/archives/2017/1485273_10469.html https://www4.tepco.co.jp/en/press/corp-com/release/betu17_e/images/171225e0213.pdf Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.5

TIP dry tube failure? Dry tubes open to containment, reach from below into core regions Free cross section of 22 lances ~9 cm 2 Highly likely that these dry-tubes get damaged by core overheating Uncertain what real leakage cross section is Failure of In-core Dry Tubes (I of II) Three Mile Island Accident of Knowledge Database NUREG/KM-0001, https://www.nrc.gov/reading-rm/doc-collections/nuregs/knowledge/km0001/r1/ Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.6

TIP dry tube failure? Dry tubes fail in ring when bypass fluid temperature > 1400 C Steam leakage Leakage of failed tubes: 10% of free area (bounding high assumption) Pipe length ~20 m, squeezed over first 20 cm, DHYD = 0.001 Failure of In-core Dry Tubes (II of II) - Highly likely that leakage occurs, but flow is expected to be too small to cause level measurement malfunctioning Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.7

Recirculation pumps seal failure? Recirculation Pump Seal Leakage (I of II) Control rod drive hydraulic system injects ~3 gpm cold water per pump into shaft seal Most enter RCS, some leaks to the outside Leakage low / high alarm < 0.25 / > 0.9 gpm per pump 1F1 equipment sump level rise -> 0.71 gpm => 0.04 kg/s per pump Sump levels Plant Data published by TEPCO https://www4.tepco.co.jp/en/nu/fukushima-np/index10-e.html Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.8 Time

In SBO condition Pump seals designed for 160 F ~71 C With loss of AC power pump seal cooling stops, possibility causing thermal damage of seals In SBO / overheating tests, no significant leakages were observed (NUREG/CR-4821) Theoretical max. leakage 100 gpm / 6 kg/s Observed operational BWR seal leakages (NUREG-1401) mostly < 10 gpm / 0.6 kg/s Recirculation Pump Seal Leakage (II of II) Steam leakage would be saturated Can not cause a dry-out of the RPV liquid level measurement - Increase of pump seal leakage in 1F1 appears currently unlikely, but not finally resolved, but it cant cause dry-out of level measurement lines Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.9

Main steam lines Transports steam from RPV to turbine 18 inch schedule 80 piping, thermally insulated Closed off by main steam isolation valves Reach ~700 C up to 21:30 on the March 11 th No continuous flow from RPV - superheated core gas can cool in steam separator & dryer Creep Rupture of Main Steam Pipe (I of II) Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.10

Creep Rupture of Main Steam Pipe (II of II) At ~ 700 C only limited creep damage ~1% creep damage up to 21:30 unlikely that pipe failed that early Simulation without MSL leakage - If main steam pipe failed early on, then likely not by rupturing but at measurement penetrations (compare LHF4, OLHF4) resulting in small leakage OECD Lower Head Failure Project Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.11

Safety relief valves Relief function by pneumatic cylinder Safety function by spring Flanged with graphite gasket (design temperature 450 C) Dump steam into suppression pool via 10 inch pipes Failure of Safety Relief Valves (I of V) TEPCO Photo & Video Library https://www7.tepco.co.jp/library/index-e.html Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.12

Failure of Safety Relief Valves (II of V) Simulation temperatures SRV body shortly above 500 C SRV mechanics cooler ~200 C up to 20:00 Why so low temperatures Non-insulated - heat loss to PCV No continuous flow from RPV - superheated core gas can cool in steam separator & dryer Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.13

SRV gasket failure? In simulation, SRV temperature (450 C) exceeded for < 15 min Exceeding the design does not mean failure > 700 C graphite gets oxidized (slowly) by steam Failure of Safety Relief Valves (III of V) - Highly unlikely that SRV gasket started leaking GRAFOIL Flexible Graphite Engineering Design Manual In gasketing conditions, the 975 F (525 C) temperature should not be considered a maximum use temperature in air but merely a caution flag that requires further examination of the operation. The thin-edge exposure of GRAFOIL packings and gaskets has successfully withstood extended periods of exposure to air at process fluid temperatures up to 1500 F (815 C). Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.14

Failure of Safety Relief Valves (IV of V) SRV stuck-open? In simulation, SRV body > 450 C for < 15 min Design exceeding, but probably able to stand heat load Stuck-open failure would not lead to a heat-up of the PCV atmosphere Inconsistent to high containment pressure - Appears unlikely that SRV failed in open position Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.15

Failure of Safety Relief Valves (V of V) Shift of actuation pressure? Relief function open 72.7 barg / close 69.7 barg relative to environment Safety function open 76.4 barg / close 68.8 barg relative to containment (PCV) atmosphere Pressure measurement at 20:07 69 barg Measured pressure just at the lower edge of the SRV safety opening band (possible but unlikely) When pressure is kept via safety valves, PCV pressure causes rise in RPV pressure Safety function defined by steel spring Heat-up reduces steel Youngs module ~ 4%/100K RPV spring temperature 150 C -> 250 C -> SRV set-points ~73 barg and 66 barg RPV pressure [bar] 80 70 60 50 40 30 Tsunami 18:25 - IC off Quake 18:18 - IC on 21:30 - IC on Paper strip record MELCOR (CVH-P.220) RPV pressure recorded data Dry-well presssure recorded data Wet-well presssure recorded data 20 10 - Likely that heat-up of SRV body caused slight decrease in actuation pressure 0 12:00 14:00 16:00 18:00 20:00 22:00 0:00 2:00 4:00 6:00 8:00 10:00 12:00 Local time [3/11/2011 hh:mm] Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.16

Indications for RCS failure long before RPV failure Malfunctioning of the RPV liquid level measurement at March 11 th 21:30 Summary (I of II) Containment pressure buildup to 6 bar-abs at 12 th March 01:00, thus before RPV failure was likely Damage to the TIP dry tubes Highly likely that damage occurred as these pipes reach within the core Unknown cross section after squeezing flat TIP failure alone cannot explain the faulty level measurement Failure of the pump seals Currently appears unlikely, but inconclusive Releases steam < 180 C, can contribute to pressure buildup, but not to dry-out of RPV level sensing lines Failure of the SRV graphite gaskets Occurrence is highly unlikely due to temperature resistance of gaskets Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.17

Failure of SRV in open position More unlikely as no extremely high temperature loads No indications of this occurrence in the containment response A fail-open would not lead to the observed liquid level measurement failure Large Rupture of main steam line due to creep Appears unlikely, especially in the early stages Can not explain the liquid level measurement failure at 21:30 Most Likely: Instrumentation penetration failure of the main steam line Small leakage of few cm 2 sufficient to cause level measurement failure when failure location in the upper containment Consistent scenario with the TEPCO Gothic analysis Additionally: Shift of the SRV pressure set-points due to heat-up Can explain the 69 bar RPV pressure measurement at 20:07 Will not lead to a substantial depressurization of the RCS, not to level malfunctioning and not to containment pressure rise Summary (II of II) OECD Lower Head Failure Project https://www.oecd-nea.org/nsd/docs/2002/csni-r2002-27.pdf Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.18

Editor and Copyright 2018: Framatome GmbH Paul-Gossen-Straße 100 91052 Erlangen, Germany. It is forbidden to reproduce the present publication entirely or partially without prior consent in whatever form. Legal action may be taken against any infringer and/or any person breaching the aforementioned conditions. Subject to change and error without notice. Illustrations may differ from the original. The contained statements and information are for advertising purposes only and do not constitute an offer of contract. They shall neither be construed as a guarantee of quality or durability, nor as warranties of merchantability or fitness for a particular purpose. These statements, even if they are future-oriented, are based on information that was available to us at the date of publication. Type, quantity and characteristics of goods and services are subject to formal individual formal contracts. Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome p.19

Thank you! Details of the Accident Progression in 1F1 BRAUN EMUG 2019-3-5.4.2019 Property of Framatome - Framatome