ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics www.europeanspallationsource.se CEC – ICMC 2015 June 29, 2015.

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Presentation transcript:

ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics CEC – ICMC 2015 June 29, 2015

View of the Southwest in  MAX IV  ESS Max IV – a national research facility, under construction, opens up in 2016 Science City – a new part of town Lund ( ) Malmö ( ) Copenhagen ( )

Cryogenics at ESS Coldbox building Compressor building

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 4

Pure Helium Gas Storage 1 20 m 3 LHe Tank Standalone Helium Purifier Helium Recovery System Pure Helium Gas Storage 2 Accelerator Cryoplant Test & Instrument Cryoplant 5 m 3 LHe Tank Target Moderator Cryoplant LHe Mobile Dewars Test Stand Distribution System Instruments & Experiments LN2 Storage Tanks LN2 Mobile Dewars Cryogenic Distribution System Cryomodules Cryomodule Test Stand Target Distribution System Hydrogen Circulation Box Hydrogen Moderator 5 (1) System overview

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 6

(2.1) The Accelerator cryogenic setup 7

8

(2.2) Cryomodule cooling at 2K 9 Production of 2 K helium in 2 K heat exchanger and a sub-sequent Joule- Thomson valve in each of the cryomodule–valve box assemblies

(2.3) The Accelerator cryoplant dutyspec 10 TypeTemperature range Max. load Stage 1 Max. load Stage 2 Static and dynamic load in CMs2 K1850 W2230 W Recuperators and CDS load2 – 4 K630 W830 W Thermal shields33 – 53 K8 550 W W Coupler cooling4.5 – 300 K6.8 g/s9.0 g/s

(2.4) The Accelerator cryogenic load 11

(2.5) The Accelerator cryoplant process K 115 K 70 K 53 K 33 K 24 K 9 K 6 K 4.5 K Compressor skids with 3 identical screws 6 turbo expanders Thermal shield ~43K Connection to 20 m 3 tank 3 cold turbo compressors VFD for SP  MP and LP  MP

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 13

14 Proton beam window Moderator and reflector plugs Target wheel Neutron beam windows Neutron beam extraction (3.1) The Target Monolith

15 (3.2) The Target Monolith inside Target wheel Proton beam window Moderator and reflector plugs

16 Target wheel Bottom MR plug Proton beam Top MR plug (3.3) Moderator-Reflector system

(3.4) The Target cryogenic load 17

(3.5) The Target Moderator cryoplant process (proposed by ESS) K 90…120 K 60…80 K 23 K 20 K 15K Helium buffers with “low” and “high” pressure region Turbine for HXs 2 screw compressor skids Intermediate “heating” of feed flow upstream turbines Helium 20.5 K 17.0 K Hydrogen 2 expansion turbines Multi purpose ambient heater

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 19

(4.1) Where sits the helium 1)ACCP: Over 2000 kg in Cryomodules and distribution system 20 2)TMCP: Over 350 kg in Cryotransferline between helium and hydrogen box 3)TICP: About 600 kg in open loop system for neutron instruments 2 x 335 m x 4”

(4.2) Helium storage 1)Pure medium pressure tanks – 19 x 67 m 3 – Theoretically up to 3.5 tons – Pressure restrictions for TICP and TMCP – Effectively ~ 3 tons 21 2)Liquid helium storage tank – 20 m 3 – When filled to 80% another 2 tons – Used as ”2nd fill” and help in transient modes (cool-down, pump-down) 3)Impure high pressure tanks or bundles – 12 m 3 – Nearly 300 kg – Used as buffer in recovery system

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 22

(5.1) Definitions 23 Kinetic Experiments Flux Integrated Experiments A reliability of at least 90% should be provided for the duration of the measurement. The measurement will be considered failed when the beam power is reduced to less than 50% of the scheduled power for more than 1/10th of the measurement length. For the duration of the experiment at least 90% of the experiments should have at least 85% of beam availability and on average more than 80% of the scheduled beam power. The beam will be considered unavailable when its power is less than 50% of its scheduled power for more than one minute. At least 90% of the users should receive a neutron beam that will allow them to execute the full scope of their experiments

(5.2) Anticipated failure rates 24 Downtime durationAcceleratorTargetICSSI 1 second - 6 seconds120 per day--- 6 seconds - 1 minute40 per day--- 1 minute - 6 minutes4.8 per day-40 per year- 6 minutes - 20 minutes 1.7 per day-10 per year- 20 minutes - 1 hour90 per year2 per year4 per year3 per year 1 hour - 3 hours29 per year1 per year2 per year1 every 2 years 3 hours - 8 hours15 per year1 every 2 years 8 hours - 1 day5.5 per year1 every 2 years1 every 5 years1 every 3 years 1 day - 3 days2.3 per year1 every 2 years-1 every 10 years 3 days - 10 days1 every 5 years1 every 20 years-- more than 10 days3 every 40 years1 every 40 years--

(5.3) Backup compressor system 25

Outline 1)System Overview 2)Accelerator Load and its Cryoplant 3)Target Moderator Load and its Cryoplant 4)Helium Management and Storage 5)Reliability and Availability 6)Energy 26

(6.1) Energy high level goals 27

(6.2) Heat recovery 28 No elevated oil or helium temperatures out of compressor suppliers specs More efficient heat exchangers, especially oil coolers Dedicated cooling water circuit for cryoplant Cooling function has priority over heat recovery Motor Middle temperature Supply Oil separator Helium compressor Helium cooler Oil cooler Helium High temperature Return Middle temperature Return 25°C 30°C 27°C 40°C 73°C 32°C 65°C 37°C 70°C Oil pump

(6.3) Energy efficiency and sustainability 29 Focus on process design and optimization Good match between plant and load by staging, dual equipment, VFDs for low pressure machines Focus on turn-down scenarios Incentive OPEX approach in ACCP and TMCP tender evaluation and contracts as well As much as possible helium recovery

Conclusions 30 The conceptual design of the cryogenic system at ESS is finished One cryoplant is ordered, one out for quote, one to 90% specified  ESS is rolling High level goals in terms of energy efficiency and sustainability can be met Continued work on meeting reliability and availability requirements