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Reactor MELCOR Model

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Proof-of-concept Gas Reactor MELCOR Model

Paul Boneham

Jacobsen Analytics

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Introduction

• Motivation: to show that a MELCOR model was possible and potentially useful for AGR

• Entirely an in-house effort by Jacobsen Analytics

• No endorsement of modelling or results from EDF Energy or ONR etc

• Model created using information available in publically accessible documents

• Nature of project leads to some limitations:

• Limited possibility to benchmark model

• Limited resource used – simple model

• References for data:

1. “Description of the advanced gas cooled reactor (AGR)”, Riso National Laboratory, Denmark, Nov 1996.

2. “VEC – A transient whole circuit model for AGRs”, paper presented at IAEA, Vienna, Dec 1985.

3. “Decay heat generation in fission reactors”, Chapter 8 of student material by M. Ragheb, Rensselaer

Polytechnic, 2011.

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Figure of AGR (from Ref. 1)

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Nodalisation – Control Volumes

Environment

Upper CPV region

Boil er gas sp ace

B oil e r – 3 s tack ed CV

Lower CPV region Gas baffle

Ann ulus Gr aph it e gaps Fue l chan ne ls 8 s tack ed CV

Two flow paths: SRV, LOCA Two flow paths:

SRV, LOCA

Feedwater To turbine

(modelled

by another

CV, not

shown)

(5)

Nodalisation – summary of heatsinks

• Heatsinks modelled:

• Boiler wall (tubes)

• Channel modelling very simplified – 8 heatsinks represent graphite sleeves in channels stacked vertically (multiplicity: 308 for each one)

• Single graphite “lump” to represent graphite bricks in core (heat conduction to sleeves modelled)

• Core support structures

• Concrete walls, ceiling and floor

• Core: no use of core package, no attempt to simulate core degradation

Fuel and clad represented using heatsinks (HS with multiplicity)

Control function for power input to UO2 pellets

8 vertical sections, ~11000 fuel pins (UO2 + Steel cladding)

• Uncertainties

• Estimated graphite heatsink dimensions based on overall core and fuel channel dimensions (fuel channel dimensions and numbers known precisely from Refs)

• Core support (diagrid) dimensions/mass not known – estimated based on overall physical dimensions of lower CPV region

• These items likely important for overall accident response

(6)

Boiler model

• Boiler modelled as three sections:

• Subcooled water

• Steam/water zone

• Superheated steam

• Used typical PWR SG tube dimensions due to lack of better information

• Important area of modelling uncertainty: lack of information on boiler design – number of tubes, orientation (coiled), heat transfer area, etc

• Tuned heat transfer area to get reasonable agreement with operating parameters

• Steady state results suggest that boiler model would need improvement

• More vertical nodes probably needed – e.g., VEC model (Ref 2) uses 10 stacked

nodes

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Steady state

• Tuning of boiler heat transfer allowed reasonable agreement with published parameters in normal operation

Parameter Value from Ref 1 Value - MELCOR Model (% error)

Gas flow through core 3680 kg/s 3732 kg/s (+1.4%)

Gas inlet temperature 565 K 592 K (+4.8%)

Gas outlet temperature 918 K 969 K (+5.5%)

Boiler temperature range (subcooled – superheated)

431 K to 813 K 486K to 636K (+12.8% to -21.8%)

(8)

Steady state

• Predicted temperatures in steady state (no comparison data available)

Parameter Value - MELCOR Model

Fuel centreline temperature (mid core) 2022K

Clad temperature (mid core) 936K

Graphite temperatures (range)* 649 K to 932 K

* Ref 1 suggests graphite temperatures in operation are above 670 K

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Transients

• TR1 – reactor, turbine, gas circulator trip. Loss of feedwater

• TR2 – 3” break in boiler steamline with loss of feedwater. Reactor, turbine and gas circulator trip.

• TR3 – primary circuit breach (1.5” diameter). Reactor, turbine,

feedwater and gas circulator trip.

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Example results will be presented at meeting

Note sensitivity to accuracy of heat sink masses and heat transfer between structures expected – i.e., heatup timescales may be significantly different to those shown here.

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Conclusions (1)

• MELCOR model considered a success, given resource and information limitations

• MELCOR can produce credible accident response and initial steady state –especially bearing in mind simplicity of modelling

• Built-in materials properties for needed fluids and structures – CO2, water, graphite, UO2, steel (clad)

• Good models for two phase water behaviour – advantage over

traditional gas reactor transient analysis codes

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Conclusions (2) - areas of modelling to improve for real application

• Areas related to information needs:

• Graphite and steel heatsink dimensions

• Boiler model

• arrangement, heat transfer area

• Roughness of fuel pins (ribbed steel cans)

• Areas related to simplified modelling:

• Arrangement of core, representation of channels

• Structure to structure heat transfer modelling (e.g., between graphite heatsink):

• Conduction modelling, review radiation HT modelling

• Severe accident simulation:

• Use of core model

• Model reduction of CO2 to CO

• Benchmarking

• Benchmark against traditional AGR code analyses

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