ITER Cryoplant Status Economics of the LHe Plants · 2018. 11. 15. · • E.g. Screw Compressor...
Transcript of ITER Cryoplant Status Economics of the LHe Plants · 2018. 11. 15. · • E.g. Screw Compressor...
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Disclaimer: The views and opinions expressed herein do not necessarily reflect those of the ITER Organization
ITER Cryoplant Status Economics of the LHe Plants
Emmanuel MONNERET M. Bonneton, M. Chalifour, E. Fauve, T. Voigt, S. Badgujar, H-S. Chang, G. Vincent ITER Organization, Route de Vinon-sur-Verdon, CS 90 046, 13067 St. Paul Lez Durance Cedex, France
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Summary
1. ITER Cryoplant Status – Cryoplant Overview – Cryoplant Project Schedule
2. Cryoplant Specifications and Constraints
3. Economics of the LHe Plants
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Summary
1. ITER Cryoplant Status – Cryoplant Overview – Cryoplant Project Schedule
2. Cryoplant Specifications and Constraints
3. Economics of the LHe Plants
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Purpose of Cryogenics
• High fields magnets
• HTS current leads
• Cryogenic pumping
• Reducing of specific project cost
• Saving energy
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Cryoplant Main Duties
• Basic – Gradual cool-down and warm-up in about one month – Provide and Recover Helium to Cryodistribution / Magnets /
Cryopumps / Thermal Shields • Maintain magnets and cryopumps at nominal temperatures over a wide
range of operating modes with pulsed heat loads due to nuclear heating and magnetic field variations
• Accommodate periodic regeneration of cryopumps – Accommodate resistive transitions and fast discharges of the
magnets and recover from them in few days – Enhanced mode to cool magnets at 3.7 K with an extended dwell time
• Additional – Ensure high flexibility and reliability – Low maintenance
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Cryogenic System Architecture
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Cryoplant System Architecture
• Main Components in the Cryoplant – LHe Plants – 3 x Plants // – 80 K helium loops - 2 x Plants in // – LN2 Plants – 2 x Plants in // and GN2 Generator and Storage – Recovery & Purification systems and Heaters – Storages – Full helium inventory in warm and cold (4.5 K and 80 K) helium tanks
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• LHe Plants: avg. 75 kW [email protected] in POS avg. mode 87 kW in refrigeration
– Superconducting magnet system, HTS current leads – Cryo-pumps with high regeneration frequency and small users
• 80K He Loops: avg. 40 kW equivalent @ 4.5 K – Thermal Shields (2 x 4000 g/s in between 80K to 100K)
• LN2 Plants: ~1300 kW @ 80 K – 80K He Loop, LHe Plants pre-cooling
• GN2 Generator: ~1550 Nm3/h – Tokamak users, Leaks, Purifier/Dryers, Air Instrument redundancy
CERN LHC: ~140 kW
ITER Cryoplant: up to 127 kW
Cryoplant He and N2 Cooling Capacities
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• Helium Storage & Inventory Management – Helium inventory: 27 t – Helium Storage
• 5 x 400 m3 of pure GHe tanks @ 300K • 1 x 175 m3 of LHe tank • 2 x 360 m3 of Quench Tanks (storage temperature ~80K) • 1 x 400 m3 of impure GHe tank @ 300K • 7 x 120 m3 of GasBags
• Nitrogen Storage & Inventory Management – LN2 inventory: 250 t – GN2 inventory: 4.5 t – Nitrogen Storage
• 1 x 300 m3 of LN2 tank • 1 x ~100 m3 of GN2 tank
Cryoplant Helium & Nitrogen Inventory
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Cryoplant Layout – Buildings 51 and 52, Area 53
• Yellow: IO Fund (PBS 34.4H Helium Plants) • Blue: Europe PA (3.4.P1.EU.01 – LN2 Plant and
Auxiliary Systems) • Green: India PA (3.4.P2.IN.02 – Cryolines and Warm
lines & 3.4.P3.IN.01 - Cryodistribution)
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CRYOPLANT PROJECT SCHEDULE
• 6 Cryogenic Contracts to manage + Interfaces (Civil work and Utilities)
• For all procurements IO is responsible for Integration and Operator
PBS # Name Resp. Procure Contractor 1st Delivery
34.10 LN2 Plants and Auxiliary Systems
F4E – Europe Air Liquide Engineering (Champigny - FR)
April 2016
34.2S Cryolines group Y (“simple” cryolines)
IN-DA - India Inox India (IN) Feb. 2016
34.2C Cryolines Group X (“complex” cryolines)
IN-DA - India Under Bid phase March. 2017
34.2W Warm lines IN-DA - India Under Bid phase Feb. 2016
34.3Y CTCB (Interconnection box) IN-DA - India Under Bid phase Jan 2017
34.4H LHe Plants IO - Cadarche ALAT (Sassenage-FR) Dec. 2015
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CRYOPLANT PROJECT SCHEDULE
• Interfaces Management and Schedule – Intense collaboration with interfaces
PBS # Interfaces Ready For Equipment
63 Civil work 2016 63 Building finishing 2017 43 Electricity 2nd semester
2016 26 Cooling water End 2016 65 Compressed Air End 2016 45 / 46 I&C Networks Mid 2016 64 / 69 Security, Environment monitoring 2017
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2010 2011 2012 2013 2014 2015 2016 2017 2018 2019 2020 2021 2022
PA PAs and Contract signature
Preliminary Design
Final Design
LHe
Plan
ts
Ready for Cryodistribution testing in Tokamak and Users
Conceptual design phase CDR CDR
Cryodistribution
LN2 P
lant
s an
d Au
xilia
ry S
yste
ms
Lines
Manufacturing
Construction
Tests
CRYOPLANT PROJECT SCHEDULE
Cryoplant Building RFE
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Summary
1. ITER Cryoplant Status – Cryoplant Overview – Cryoplant Project Schedule
2. Cryoplant Specifications and Constraints
3. Economics of the LHe Plants
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Cryoplant Specifications and Constraints
• State-of-the-art technology adapted to large dynamic loads and parallel refrigerators operation
• High availability and reliability – RAMI
• Investment and personal protection – HAZOP – SIL Study
• Operation costs optimization – Overall process cycle and components efficiency – Compressors heat recovery for hot water distribution – Gas Nitrogen generator on site to produce and distribute GN2 – Liquid nitrogen pumps to regulate liquid nitrogen distribution
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• Regulatory requirements – French Decree No. 99-1046 – Pressure Vessels – French Quality Order - Nuclear environment
• Codes – Mainly pressures vessels according to PED
• Issues: periodic inspection and requalification, use CTP and BSEI in order to proper implement counter measures
• Standards – Reliability
• E.g. Screw Compressor (ISO EN 10440-1, equivalent to API 619) • All rotating machineries (centrifugal compressor, pumps, etc.) • Heat Exchanger (TEMA and ALPEMA)
– Standardization • International project • Minimize costly operation, maintenance and spares management
Cryoplant Specifications and Constraints
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Summary
1. ITER Cryoplant Status – Cryoplant Overview – Cryoplant Project Schedule
2. Cryoplant Specifications and Constraints
3. Economics of the LHe Plants
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Economics of the LHe Plants
• Economics of the ITER LHe Plants based on: – Contract for 3 identical LHe Plants pre-cooled with LN2 – Lump Sum Turn Key Contract [LSTK] ~EPCI + Commissioning – Excluded
• Civil work, buildings utilities and security • Electricity (Main distribution board) • Cooling Water • Compressed Air
• Economics studies based on refrigeration power
ITER LHe Plant
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Economics of the LHe Plants • Green Formula [1997]
• CERN-LHC Formula [1999]
• Green Formula [2007]
• ITER [2014]
Coef. [2.6] not enough data to be assessed
𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑀𝑀𝑀 = 2.6 ∗ (𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑘𝑘𝑘𝑘𝑘𝑘.5𝐾𝐾 )0.7
𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 1998𝑀𝑀𝐶𝐶𝑀𝑀𝑀𝑀 = 2.2 ∗ (𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑘𝑘𝑘𝑘𝑘𝑘.5𝐾𝐾 )0.6
𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑀𝑀𝑀 = 2.6 ∗ (𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑘𝑘𝑘𝑘𝑘𝑘.5𝐾𝐾 )0.63 𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑀𝑀€ = 2.6 ∗ (𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶𝐶 𝑘𝑘𝑘𝑘𝑘𝑘.5𝐾𝐾 )0.65
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Economics of the LHe Plants
• Confirmation of Green and CERN economics up to 29kW
• Proper tool for pricing at conceptual design phase
Eq. Ref. capacity @4.5K [kW] Investment cost
ITER LHe Plant (one Plant) 29 23.5 M€ Control Syst. (PLC & PIS) +5.0% Machine Monitoring System (Rotating Machinery vibration, measurement and analysis)
+1.5%
Heat Recovery System – HRS +6.5% Test Tools (fixed for 1 or 3 plants) +9.0% Capital Spares – Compressors/Turbines/Oil pumps (fixed for 1 or 3 plants) +2.0%
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Economics of the LHe Plants • Heat Recovery System [HRS]
– Heat recovered from compressor oil – Heat transferred to “Hot Water” for ITER
buildings heating syst. (electrical boiler as back-up)
– Studies and Design based on ITER scenario
• 16 months operation (+2 for CD and WU) • Heaters “ON” 6 months/year
• Average estimated power recovered ~8 MW for 12MW installed
• Payback after Tokamak commissioning phase
• Highly recommended to study power recovering on large refrigeration plant
CCWS2
Hot Water Loop
HeliumHelium + Oil
Oil
45°C
TT
TT
Setpoint: 40°C
TT100°C (TBC)
FT
FT
V1
V2
TBC: To be confirmed
95°C
32°C 42°C
EX1
EX2
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Page 22 IDM UID: NC5BC5
Disclaimer: The views and opinions expressed herein do not necessarily reflect those of the ITER Organization
ITER Cryoplant Status Economics of the LHe Plants
Emmanuel MONNERET M. Bonneton, M. Chalifour, E. Fauve, T. Voigt, S. Badgujar, H-S. Chang
ITER Organization, Route de Vinon-sur-Verdon, CS 90 046, 13067 St. Paul Lez Durance Cedex, France
Thanks for Your Attention
Particular thanks to: • The cryogenic section colleagues • The Domestic Agencies (F4E and ITER India)