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

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

Transcript of ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics CEC – ICMC 2015 June...

Page 1: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

ESS Cryogenic System Process Design

Philipp ArnoldSection Leader Cryogenics

www.europeanspallationsource.seCEC – ICMC 2015

June 29, 2015

Page 2: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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View of the Southwest in 2025

MAX IV

ESS

• Max IV – a national research facility, under construction, opens up in 2016

• Science City – a new part of town

Lund(113 500)

Malmö(309 000)

Copenhagen(1 200 000)

Page 3: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

Cryogenics at ESS

Coldbox building Compressor building

Page 4: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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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

Page 5: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

Pure Helium Gas Storage 1

20 m3 LHe Tank

Standalone Helium Purifier

Helium Recovery System

Pure Helium Gas Storage 2

AcceleratorCryoplant

Test & Instrument Cryoplant

5 m3 LHe Tank

Target ModeratorCryoplant

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

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(1) System overview

Page 6: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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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

Page 7: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(2.1) The Accelerator cryogenic setup

Page 8: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(2.1) The Accelerator cryogenic setup

Page 9: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(2.2) Cryomodule cooling at 2K

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

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(2.3) The Accelerator cryoplant dutyspec

Type Temperature range

Max. loadStage 1

Max. loadStage 2

Static and dynamic load in CMs 2 K 1850 W 2230 W

Recuperators and CDS load 2 – 4 K 630 W 830 W

Thermal shields 33 – 53 K 8 550 W 11 380 W

Coupler cooling 4.5 – 300 K 6.8 g/s 9.0 g/s

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(2.4) The Accelerator cryogenic load

10 15 20 25 30 35 40 45 50 55 600

500

1000

1500

2000

2500

3000

3500ACCP 2K heat load vs number of installed CMs

Beam ON w/ safety factorsBeam ON w/o safety factorsBeam OFF w/ safety factorsBeam OFF w/o safety factors

Number of Cryomodules

ACCP

2K

heat

load

, W

Beam commissioning

Medium beta CM complete

High beta CM 1-11 complete

Optimus+High beta CM com-

plete (Stage 1)

Optimus+ contin-gency

High beta CM com-plete (Stage 2)

Page 12: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(2.5) The Accelerator cryoplant process

300 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 m3 tank

3 cold turbo compressors

VFD for SPMP and LPMP

Page 13: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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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

Page 14: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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Proton beam windowModerator and reflector plugs

Target wheel

Neutron beam windows

Neutron beam extraction

(3.1) The Target Monolith

Page 15: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(3.2) The Target Monolith inside

Target wheel

Proton beam windowModerator and reflector plugs

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Target wheel

Bottom MR plug

Proton beam

Top MR plug

(3.3) Moderator-Reflector system

Page 17: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(3.4) The Target cryogenic load

0 1 2 3 4 5 60

5

10

15

20

25

30

35TMCP 15-20K heat load vs. beam power

Load w/ safety factorsLoad w/o safety factors

Beam power, MW

TMCP

hea

t loa

d, k

W

Beam OFFBeam

commissioningMedium beta CM complete

High beta CM 1-11 complete

Nominal designHigh beta CM com-

plete

Page 18: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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(3.5) The Target Moderator cryoplant process (proposed by ESS)

300 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

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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

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(4.1) Where sits the helium

1) ACCP: Over 2000 kg in Cryomodules and distribution system

NO CD0

500

1000

1500

2000

2500

Helium mass in CMs & CDS w/o shield[kg]

Vapour Helium

Liquid Helium

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”

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(4.2) Helium storage

1) Pure medium pressure tanks– 19 x 67 m3

– Theoretically up to 3.5 tons– Pressure restrictions for TICP and TMCP– Effectively ~ 3 tons

2) Liquid helium storage tank– 20 m3

– 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 m3

– Nearly 300 kg – Used as buffer in recovery system

Page 22: ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics  CEC – ICMC 2015 June 29, 2015.

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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

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(5.1) Definitions

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

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(5.2) Anticipated failure rates

Downtime duration Accelerator Target ICS SI

1 second - 6 seconds 120 per day - - -

6 seconds - 1 minute 40 per day - - -

1 minute - 6 minutes 4.8 per day - 40 per year -

6 minutes - 20 minutes 1.7 per day - 10 per year -

20 minutes - 1 hour 90 per year 2 per year 4 per year 3 per year

1 hour - 3 hours 29 per year 1 per year 2 per year 1 every 2 years

3 hours - 8 hours 15 per year 1 every 2 years 1 every 2 years 1 every 2 years

8 hours - 1 day 5.5 per year 1 every 2 years 1 every 5 years 1 every 3 years

1 day - 3 days 2.3 per year 1 every 2 years - 1 every 10 years

3 days - 10 days 1 every 5 years 1 every 20 years - -

more than 10 days 3 every 40 years 1 every 40 years - -

Not relevant for the

cryogenic system

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(5.3) Backup compressor system

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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

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(6.1) Energy high level goals

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(6.2) Heat recovery

• 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

32°C 65°C

37°C

70°C

Oil pump

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(6.3) Energy efficiency and sustainability

• 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

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Conclusions

• 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