ARIES Meeting General Atomics, February 25 th , 2005 Brad Merrill, Richard Moore Fusion Safety Program Pressurization Accidents in ARIES- CS
Jan 08, 2016
ARIES Meeting General Atomics, February 25th, 2005
Brad Merrill, Richard MooreFusion Safety Program
Pressurization Accidents in ARIES-CS
Presentation Outline
• Describe the details of a MELCOR model under development for the ARIES-CS dual coolant blanket concept
• Present MELCOR results for reactor startup
• Present the results of a decay heat removal analysis for a complete loss-of-flow-accident (CLOFA) as a benchmarking exercise for our MELCOR model
• Discuss possible accident scenarios that must be considered in assessing the safety of ARIES-CS
• Present results for two vacuum vessel (VV) pressurization accidents with the use of the ARIES-CS MELCOR model
• Conclude by discussing future modeling requirements and analyses
Modeling Assumptions and Parameters
• Modeled one-half a field period segment (1/6th of three field period reactor)– First wall surface area 1/6 of plasma surface area ~ 135 m2
– Applied first wall heat flux of 0.5 MW/m2
– Total operating thermal power for model ~ 372 MW
– Decay heat (obtained from “Initial Activation Assessment for ARIES Compact Stellarator Power Plant” paper ~ 10 MW at shutdown and 3 MW at 60 s)
– Radial build based on Laila’s Nov. 11th radial compositions and an ARIES-ST unit blanket cell
• Helium Loop (~115 m3)– Pressure 8 MPa and inlet /outlet temperature 300/480 °C
– Mass ratio (external /in-vessel) ~ 7 to maintain He velocities below 40 m/s in piping
• PbLi Loop (~255 m3)– Pressure 4 MPa and inlet /outlet temperature 460/700 °C
– Mass ratio (external /in-vessel) ~ 4 (assumed from previous studies)
• Loop configurations based on ARIES-AT confinement building
Header
PbLi drain tank
Heat transfer vault
HXs
Pump
Circ.
MELCOR Model Elevations Based on ARIES-AT
(Need similar information for ARIES-CS)
MELCOR ARIES-CS Model Schematic
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He toroidal header
He concentric pipe PbLi toroidal header
PbLi concentric pipe
PbLi heat exchanger
He heat exchanger
IB Shield
VV VV
IB blanket OB blanket OB Shield
FW FW
Zone 1 Zone 2
Startup Transient Predictions
Fluid temperatures Structure temperatures
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dT/dt ~ 0.8 °C/sPWRs allow ~.008 °C/s => ~ 4 MW to heat loops
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CLOFA Decay Heat Removal
• Shutdown and complete loss of active cooling flow occurs, with the VV cooling system entering a natural convection mode
• Latent heat re-distribution results in FW temperature of ~ 630 °C (lower than 730°C predicted by Carl, perhaps due to flow coast down)
• By 3 hours the temperatures start to decay
• At ~26 hours the PbLi loop natural convection increases
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Possible Reference Accidents
• In-vessel helium or water loss-of-coolant accident (LOCA) analysis to demonstrate:
– Pressurization does not fail first confinement barrier (i.e., ARIES-CS vacuum vessel)
– Limited chemical reactions and hydrogen formation (exclude water or limit PbLi)
• In-blanket (breeder zone) helium LOCA analysis to assess:– Blanket and tritium purge gas system pressurization
– Subsequent in-vessel leakage
• Ex-vessel helium and PbLi LOCA analysis to determine:– Pressurization of reactor or HTS vault is tolerable
– Behavior of FW/blanket without active plasma shutdown
• These accidents are the most likely confinement bypass event initiators because of confinement barrier over-pressurization; it must be demonstrated that for all three events the dose at the site boundary does not exceed 10 mSv for all radioactive sources combined (dust, FW oxidation, Po-210, and tritium)
Pressurization of Module Maintenance Vacuum Vessel
• Two pressurization accidents were considered
• A single FW channel rupture (0.0012 m2)
• Helium inlet header (0.04 m2)
• Design basis events with probabilities in the ~ 1x10-3/year range
• Free volume within the vacuum vessel (VV) was set at plasma volume of ~535 m3
• Immediate plasma shutdown occurs, but radiant collapse was not included
Pressurization of Module Maintenance Vacuum Vessel
• Shutdown and loss-of-coolant occurs after 1 hour, and VV cooling enters natural convection mode
• Pressures reach > 18 atmospheres within seconds after the large break while the small break takes ~ 5 minutes to reach 18 atmospheres
• A pressure relief system will be required for this VV option
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Pressurization of Period Maintenance Vacuum Vessel
• Two pressurization accidents were considered
• A single FW channel rupture (0.0012 m2)
• Helium inlet header (0.04 m2)
• Design basis events with probabilities in the 1x10-3/year range
• Free volume within the vacuum vessel (VV) was set at plasma volume of ~7000 m3
• Immediate plasma shutdown occurs, but radiant collapse was not included
• Shutdown and loss-of-coolant occurs after 1 hour, and VV cooling enters natural convection mode
• Pressures reach ~ 2.0 atmospheres within seconds for the large break while the small break takes ~ 10 minutes to reach 2.0 atmospheres
• A pressure relief system may not be required for this VV option
• However, decay heat removal may be an issue
Pressurization of Period Maintenance Vacuum Vessel
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Results Summary
• A decision must be made on which accidents will be selected as Reference Accident Scenarios (pressurization, decay heat removal, and hydrogen generation are concerns)
• Models are being developed to analyze releases during adopted Reference Accident Scenarios, but more design information and benchmarking is required
• Decay heat removal analysis suggests temperatures somewhat less than Carl’s analyses, and this difference must be investigated further
• The VV is the primary confinement barrier and design basis pressurization events must not fail this boundary
– The small VV for the module maintenance scheme will not work without an expansion volume available (will also be part of primary confinement boundary)
– The large VV for the sector maintenance scheme is very attractive as a primary confinement barrier, if the decay heat removal problem can be addressed
Future Analysis Requirements
• MELCOR in-blanket (LOCA) model may have to be developed based on choice of tritium and Po-210 (or Bi-208) extraction systems (low or high pressure extraction systems)
• Tritium inventory, permeation, and accident releases
– Annual release limit (0.1 g-T as HTO/a – ITER to 8 g-T as HTO/a – FIRE) translates into an in-building permeation limit of between ~10 to 800 g-T/a, assuming a 99% efficient tritium cleanup system
– To meet this limit the tritium extraction method proposed by Siegfried Malang, which is a vacuum permeator (Nb tubes), is proposed for the PbLi to lower the T2 concentration to levels (produce pressures above PbLi < 0.2 Pa) where losses to the building are below the annual release limit
– Will need tritium production rates
• A TMAP model should be developed to examine tritium permeation in the blanket and from the cooling systems, and to estimate tritium accident mobilization rates
• Need estimates of VV PFC erosion dust and FW activation product inventories
• ARIES-AT PFC dust and Po-210 inventories will be used for accident source terms
• This information will feed into MELCOR LOCA and LOVA predictions for radioactive release estimates and site boundary dose predictions