Safety Issues for High Temperature Gas Reactors Andrew C. Kadak - - PowerPoint PPT Presentation

safety issues for high temperature gas reactors
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Safety Issues for High Temperature Gas Reactors Andrew C. Kadak - - PowerPoint PPT Presentation

Safety Issues for High Temperature Gas Reactors Andrew C. Kadak Professor of the Practice Major Questions That Need Good Technical Answers Fuel Performance Normal operational performance Transient performance Ejected Rod


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SLIDE 1

Safety Issues for High Temperature Gas Reactors

Andrew C. Kadak Professor of the Practice

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SLIDE 2

Major Questions That Need Good Technical Answers

  • Fuel Performance

– Normal operational performance – Transient performance

  • Ejected Rod (maximum energy insertion capability)
  • Reactivity insertions (seismic, water)

– Accident Performance – Weak fuel issues – Mechanistic source term for high burn-up fuel – Fuel fabrication quality assurance

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SLIDE 3
  • Risk Dominant Accident Sequences

– Establish risk informed design to identify risk dominant accident sequences to be analyzed. – Use either IAEA1 or NRC2 risk informed approach to establish safety requirements of plant. – Use of safety goal as a design guide – Application of risk informed “Defense in Depth” – Scope of risk analysis may be easier due to inherent robustness of basic design.

  • 1. “Development of Technology Neutral Safety Requirements for Innovative Reactors”, IAEA

TECDOC Draft Dec. 2004 2. “Regulatory Structure for New Plant Licensing, Part 1: Technology Neutral Framework, Dec. 2004, Draft, US NRC.

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SLIDE 4

Consequences F

Initiating Event/Y

  • Lev. 1
  • Lev. 2
  • Lev. 3
  • Lev. 4
  • Lev. 5

10-2 10-6 10-7

Failure of Level 1 Initiating Event

Minimal emergency actions beyond defined distance from the plant No off-site actions beyond defined distance from the plant Off-site Actions NOTE 2: Doses are derived from IAEA-SS No 115 5 mSv/a (For 1 year period following the accident) 5 mSv/a (For 1 year period following the accident) 5 mSv/a 1 mSv/a (average 5 y) 1 mSv/a (10 µ Sv/a –target) Doses to the public NOTE 1: Doses for NO, AOO, AC are derived from IAEA-SS No 115 500 mSv (limit) (This value derived from Finnish regulation) 50mSv/a (Could be exceeded for rear recovery events) 50 mSv/a 20 mSv/a (average 5 y) (5 mSv/a target) 50 mSv/a ALARA (5 mSv/a target) Doses to Operators Severe plant conditions* (SSPC) Accident conditions (AC) Anticipated Operational Occurrences (AOO) Normal Operations (NO) Plant conditions Consequences

AOO AC SPC Challenges DESIGN BASIS * Severe challenge to the Fission Products Confinement Function

Risk Informed Safety Profile

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SLIDE 5

LEVELS OF DEFENCE IN DEPTH (From INSAG-10)

Control, limiting and protection systems Level 2 Control of deviations from normal

  • peration and detection of failures

and other surveillance features Objective Levels of defence Essential means Level 1 Prevention of deviations from normal

  • peration and failures

Conservative design and high quality in construction and operation Level 3 Control of accident conditions within the design basis Engineered safety features and accident procedures Level 4 Control of severe plant conditions Complementary measures and accident management Level 5 Mitigation of radiological consequences

  • f significant releases of radioactive

materials Off-site emergency response Acceptable failures of the Level of Defence

(events/year) < 10-2 10-2- 10-6 10-6- 10-7 < 10-7

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SLIDE 6
  • Expected Significant Accident Sequences

– Air Ingress – Water Ingress (reactivity insertion) – Seismic Events (reactivity insertion) – Loss of Load – Rod Ejection (more significant in block reactors) – Failure of reactor cavity cooling system – Recuperator By-pass events (overcooling) – Graphite dust, plate-out, lift off – Impact of Terrorism – Identification of “cliff edge” effects

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SLIDE 7

Knowledge Required

  • Improved understanding of core behavior
  • Improved understanding of heat transfer in core and vessel
  • pebble and block - bypass flows
  • Materials behavior at high temperature in helium (plus

contaminants) including radiation effects and chemical attack on graphite

  • Blow down loads and timing of accident event sequences.
  • Behavior of fuel, fission product release behavior in

reactor building and structures under accident conditions.

  • Development and validation of computer codes used in the

analysis

  • Validation of passive performance of safety systems -

natural circulation - heat conduction and convection.

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SLIDE 8

Issues

  • Fuel Temperature limits (1600 C ?)
  • Regulatory Credit for Basic Design

Strengths

  • Need new risk informed licensing process

to allow credit for innovative systems.

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SLIDE 9

Containment

  • Based on design and accident analysis of source

term and sequences - a containment of radioactive materials strategy is developed to assure that safety goals are met. – Full pressure containment – Confinement - low pressure - not pressure tight – Dynamic containment/confinement (time dependent) – Performance is quite different than water reactors.

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SLIDE 10

Classification of Safety “Systems”

  • Ideally safety system classification should

be done on importance to safety function in a risk informed manner.

  • Some “systems” are not components but

parameters in analysis for passive performance (ex. emissivity of reactor vessel).

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SLIDE 11

Expectations

  • Water Ingress - generally understood and can be

limited by amount of water ingress - some German experience at AVR

  • Seismic - reactivity simulations can assess reactivity

impact.

  • Rod ejection - more significant for block reactors but

fuel energy limits like for LWRs can be established for rod worths.

  • Testing on heat transfer and flow can be verified by

South African tests and Chinese pebble bed reactor including reactor cavity cooling systems.

  • Fuel behavior data to be provided by past German and

focused South African and US testing programs

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SLIDE 12

Challenges

  • Verification of high temperature material

behavior (fuel, graphite, metals, carbides)

  • Validation of analysis tools
  • Air ingress

– Most visible concern among the public – Most significant in terms of potential offsite consequences – Can not be eliminated by “design”

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SLIDE 13

Air Ingress Status

  • Most “eliminate” connecting “vessel”

failure as too low a probability event (10-8).

  • Break sizes limited to largest connecting

“pipe”.

  • Two breaks (top and bottom) considered

unlikely but are analyzed (chimney effect)

  • Graphite corrosion behavior not well

modeled in existing codes.

  • CFD analysis and confirmatory experiments

needed.

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SLIDE 14

Air Ingress Tests

  • Japanese series on prismatic configuration

– Diffusion – Natural Circulation – Corrosion (multi-component)

  • German NACOK tests - pebble bed

– Natural circulation – Corrosion

  • MIT CFD (Fluent Methodology Development)
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SLIDE 15

Experimental Apparatus - Japanese

C4 2 7

Nitrogen Helium Valves

C3 C1 C2 H4 H3 H2 H1

Figure 16: Apparatus for Isothermal and Non-Isothermal experiments Figure 17: Structured mesh

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SLIDE 16

Isothermal Experiment

0.00 0.20 0.40 0.60 0.80 50 100 150 200 250 300 Time (min) Mole fraction

H-1 & C-1(Calculation) H-2 & C2 (Calculation) H-3 & C3 (Calculation) H-4 & C4 (Calculation) H-1 & C-1(Experiment) H-2 & C2 (Experiment) H-3 & C3 (Experiment) H-4 & C4 (Experiment)

Figure 18: Mole fraction of N2 for the isothermal experiment

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SLIDE 17

Thermal Experiment

Figure 19: The contour of the temperature bound4ary condition

Pure Helium in top pipe, pure Nitrogen in the bottom tank N2 Mole fractions are monitored in 8 points

  • Hot leg heated
  • Diffusion Coefficients as a

function of temperature

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SLIDE 18

Thermal Experiment

0.2 0.4 0.6 0.8 1 50 100 150 200 Time (min) Mole fraction of N2

H-1(FLUENT) C-1(FLUENT) H-1(Experiment) C-1(Experiment)

Figure 20: Comparison of mole fraction of N2 at Positions H-1 and C-1

0.2 0.4 0.6 0.8 1 50 100 150 200 Time(min) Mole Fraction

H2(Experiment) C2(Experiment) H-2(FLUENT) C-2(FLUENT)

Figure 21: Comparison of mole fraction

  • f N2 at Positions H-2 and C-2
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SLIDE 19

Thermal Experiment (Cont.)

0.2 0.4 0.6 0.8 1

50 100 150 200 250

Time(min) Mole Fraction of N2 H4(Exp) C4(Exp) H-4(Calc) C-4(Calc)

Figure 22: Comparison of mole fraction

  • f N2 at Positions H-1 and C-1
  • 0.15
  • 0.10
  • 0.05

0.00 0.05 0.10 0.15 0.20 0.25 2 4 6 Time (Second) Velocity (m/second)

Figure 23: The vibration after the

  • pening of the valves.
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SLIDE 20

Multi-Component Experiment

2 1 3 4

Heated Graphite Air Helium

Graphite Inserted Multiple gases: O2, CO, CO2, N2, He, H2O Mole fraction at 3 points are measured Much higher calculation requirements Diffusion Coefficients

Figure 34: Apparatus for multi- Component experiment of JAERI

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SLIDE 21

Multi-Component Experiment(Cont.)

0.00 0.03 0.06 0.09 0.12 0.15 0.18 0.21 20 40 60 80 100 120 140 Time(min) Mole Fraction O2(Experiment) O2(Calculation) CO(Experiment) CO(Calculation) CO2(Experiment) CO2(Calculation) Figure 36: Mole Fraction at Point-1 (80% Diffusion Coff.)

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SLIDE 22

Multi-Component Experiment(Cont.)

Figure 37: Mole Fraction at Point-3

0.00 0.04 0.08 0.12 0.16 0.20 0.24 20 40 60 80 100 120 140 Time(min) Mole Fraction

O2(Experiment) O2(Calculation) CO(Experiment) CO(Calculation) CO2(Experiment) CO2(Calculation)

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SLIDE 23

Multi-Component Experiment(Cont.)

Figure 38: Mole Fraction at Point-4

0.00 0.05 0.10 0.15 0.20 0.25 20 40 60 80 100 120 140 Time (min) Mole Fraction O2(Experiment) O2(Calculation) CO(Experiment) CO(Calculation) CO2(Experiment) CO2(Calculation)

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SLIDE 24

NACOK Natural Convection Experiments

Figure 39: NACOK Experiment

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SLIDE 25

Boundary Conditions

Figure 41: Temperature Profile for one experiment

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SLIDE 26

The Mass Flow Rates

Figure 42: Mass Flow Rates for the NACOK Experiment 0.0E+00 1.0E-03 2.0E-03 3.0E-03 4.0E-03 100 300 500 700 900 1100 Temperature of the Pebble Bed (C) Mass Flow Rate (kg/s 5.0E-03 )

T_R=200 DC(Exp.) T_R=400 DC(Exp.) T_R=600 DC(Exp.) T_R=800 DC(Exp.) T_R=200 DC(FLUENT) T_R=400 DC(FLUENT) T_R=600 DC(FLUENT) T_R=800 DC(FLUENT)

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SLIDE 27

Future NACOK Tests

  • Blind Benchmark using MIT methodology

to reproduce recent tests.

  • Update models
  • Expectation to have a validated model to be

used with system codes such as RELAP and INL Melcor.

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SLIDE 28

Air Ingress Mitigation

  • Air ingress mitigation strategies need to be

developed

– Realistic understanding of failures and repairs – Must be integrated with “containment” strategy to limit air ingress – Short and long term solution needed

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SLIDE 29

Overall Safety Performance Demonstration and Validation

  • China’s HTR-10 provides an excellent test bed for

validation of fundamentals of reactor performance and safety.

  • Japan’s HTTR provides a similar platform for

block reactors.

  • Germany’s NACOK facility vital for

understanding of air ingress events for both types.

  • PBMR’s Helium Test Facility, Heat Transfer Test

Facility, Fuel Irradiation Tests, PCU Test Model.

  • Needed - open sharing of important technical

details to allow for validation and common understanding.

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SLIDE 30

Chinese HTR-10 Safety Demonstration

  • Loss of flow test

– Shut off circulator – Restrict Control Rods from Shutting down reactor – Isolate Steam Generator - no direct core heat removal only but vessel conduction to reactor cavity

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SLIDE 31

Video of Similar Test

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SLIDE 32

Loss of Cooling Test

Power

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SLIDE 33

Loss of Cooling Test

Power

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SLIDE 34

Summary

  • Safety advantages of High Temperature

Reactors are a significant advantage.

  • Air ingress most challenging to address
  • Fuel performance needs to be demonstrated in
  • perational, transient and accident conditions.
  • Validation of analysis codes is important
  • Materials issues may limit maximum operating

temperatures and lifetimes of some components.

  • International cooperation is essential on key

safety issues.