22.033 core group- reactor core and secondary design · shaped liquid metal cooled reactors...
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22.033 Core Group- Reactor Core and Secondary Design
Robert Drenkhahn Brendan Ensor Jessica Hammond Ruaridh Macdonald
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Overview
• Proposed Design & Specs
• Core
• Secondary
• Next Steps
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Preliminary Design
• Lead Cooled Fast Reactor with Supercritical CO2 Secondary Loop
• 1000 MWt (~450 MWe)
– Limited by velocity of LBE (2.5-3 m/s) currently we are using 2.5 m/s
– Subject to changes as ΔT and flow area changes (working on upping it to ~1200 MWt)
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Preliminary Design
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Black- Fuel Regions (UO2) Purple- Control Rods (B4C) Beige- Reflector (MgO) Red- Shield (B4C) Orange- Coolant (LBE) Note the Blue containment is not the actual containment (in reality it is larger)
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Preliminary Design
• Picture of Whole System
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Core Design Process
• Used MCNP (Monte Carlo N-Particle) code to design reactor
• Based off of other similar hexagon core shaped liquid metal cooled reactors (STAR-LM, ELSY)
• Design Iterations
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Iteration 1
• Version 1.0, looked at a lot of reference designs and created something similar
• See if it were critical
• Fuel Pin design: fuel LBE gap protective clad T91 protective clad coolant
• It had the whole range of S/D with rods in and supercritical with rods out – Needed less reactivity at top of core (helps with S/D margin) – Needed less power peaking in the middle
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Iteration 1
Control Rods Keff (+- 0.0005)
In 0.96822
25% out 1.01184
50% out 1.08764
75% out 1.11812
Full Out 1.3265
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Iteration 2
• Added Axial Zoning to fix the large excess reactivity (20% enriched Lower, 15% enriched Middle, 10% enriched bottom)
• Added Radial Zoning to get a flatter flux profile (Added 5% to the outer rings)
Control Rods In 0.25 0.5 0.75 Out
Keff 0.95387 1.08059 1.15039 1.16142 1.16144
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Iteration 2
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• Black- Fuel Regions (UO2)
• Purple- Control Rods (B4C)
• Beige- Reflector (MgO)
• Red- Shield (B4C)
• Orange- Coolant (LBE)
• Blue- Cladding (T91 stainless steel, protective outer layer)
• Note the Blue containment is not the actual containment (in reality it is larger)
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Iteration 2
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Iteration 2
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Power Calculation
• Used Power= ṁ cp ΔT
• Where ṁ = ρ v A
• Where v is limited at 2.5 m/s, rho is 10500 kg/m3
, A is the cross sectional coolant flow area, cp is 150 J/kg·K and ΔT is the temperature change across the core
• Directly proportional to A and ΔT
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Decay Heat Removal
• After a month of shutdown from long operation still producing about 3 MWt of energy
• After a month of shutdown from 1 month of operation still producing 400 kWt of energy
• Need to see how much power produced is sufficient to keep LBE liquid and then work with process heat
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Secondary System
• Modeled in EES
– Temperature and mass flow calculations
• Initial Assumptions Made
– Heat exchanger input and output for S-CO2
– Low end temperature after condenser
• Allows for faster optimization in the future
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Secondary System
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Secondary System
• More S-CO2 data required to perform analysis of pressure changes. – Enthalpy Tables
• Possible second loop with an added re-heater and compressor to account for changes in specific heat
• Energy diverted to Process-Heat needs to be accounted for – Only majorly effects electricity generated
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Brayton Cycle: Quick Overview
QuickTime™ and a decompressor
are needed to see this picture.
Source: UC Davis ChemWiki, license CC BY-NC-SA 3.0
http://chemwiki.ucdavis.edu/@api/deki/files/13235/=TS_Curve.jpg
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LBE & S-CO2 Heat Exchanger
QuickTime™ and a decompressor
are needed to see this picture.
© Heatric. All rights reserved. This content is excluded from our CreativeCommons license. For more information, see http://ocw.mit.edu/fairuse.
•http://www.heatric.com/
Printed Circuit Heat Exchanger (PCHE) vs. Shell-
and-Tube Heat Exchanger
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PCHE
•Compact design
•Competitive Efficiency
•Friction Factor for LBE becomes obstacle
© American Nuclear Society and the authors. All rights reserved.This content is excluded from our Creative Commons license. Formore information, see http://ocw.mit.edu/fairuse.
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Shell-and-Tube Heat Exchanger
• Simple design (easy to make, low cost, etc.)
• Larger than PCHE
• Competitive efficiency
QuickTime™ and a decompressor
are needed to see this picture.
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© Sulzer Chemtech USA, Inc. All rights reserved. This content is excluded from ourCreative Commons license. For more information, see http://ocw.mit.edu/fairuse.
http://www.thermopedia.com/content/1211/?tid=104&sn=1410
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Next Step
• Secondary: Better data, more accurate values, possible second re-heater/compressor loop, and process heat removal
• Core: Natural Circulation, Decay heat work, continue optimizing core zoning, thermal analysis of fuel
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QUESTIONS?
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