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Development of a low-pressure helium compression control strategy - - PowerPoint PPT Presentation

Development of a low-pressure helium compression control strategy for CMTF Ruslan Nagimov, BMSTU/E4 Supervisors: Arkadiy Klebaner, Jay Theilacker FNAL/AD/ENG/CRYO Summer students meeting, PARTI Program, FNAL August 29, 2012 1 Fermilab Cryomodule


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Development of a low-pressure helium compression control strategy for CMTF

Ruslan Nagimov, BMSTU/E4 Supervisors: Arkadiy Klebaner, Jay Theilacker FNAL/AD/ENG/CRYO

Summer students meeting, PARTI Program, FNAL August 29, 2012

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Fermilab Cryomodule Test Facility

Fermilab Cryomodule Test Facility (CMTF) provides a test bed to measure the performance of cryomodules and SRF cavities for future accelerators (Project X, ILC, Muon Collider).

2 Development of a low-pressure helium compression control strategy for CMTF

CMTF Refrigerator

  • Must be capable to operate efficiently
  • ver a wide range of heat loads.
  • Will be more energy efficient than any

superfluid helium cryogenic system currently in operation in Fermilab.

  • It is being designed as a one-size-

fits-many cryogenic plant for the laboratory’s future research projects.

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The Key is the Hybrid Cryogenic Cycle

  • Use both warm and cold compression
  • Efficient cryogenic capacity turndown is accomplished by

adjusting a cryogenic system helium mass flow rate to match the heat load generated by SRF components.

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Three Cold Compressor Units (CCU) – hydrodynamic machines Warm Vacuum Compressor – positive displacement machine WVC

Development of a low-pressure helium compression control strategy for CMTF

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Why Cold Compressors?

  • Cold pumping allows

recuperate cold before helium re-cooling → increasing

  • verall efficiency
  • The cold helium has a higher

density → decreasing number

  • f compression stages
  • A compressor stage can have

characteristics corresponding to optimal helium suction conditions → increasing adiabatic efficiency

Why Not Only Cold Compressors?

  • Cold compressor set has the

fixed pressure ratio → decreasing working mass flow range

  • Limited turndown capability →

decreasing efficiency

Cold & Warm Compressors

4 Development of a low-pressure helium compression control strategy for CMTF

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Cold & Hybrid Cycles Comparison

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Heat Load WVC CC CC CC Multistage cold compressors – “cold” compression cycle Heat Load CC CC CC CC Cold compressors in series with warm compressor – “hybrid” cycle

mass flow rate pressure ratio interstage pressure volumetric flow rate THe = 2.0 K THe = 1.9 K THe = 1.8 K

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Mass Flow Rate Reduction Capability

6 Development of a low-pressure helium compression control strategy for CMTF

“Cold” cycle: pressure ratio ≈ const “Hybrid” cycle: pressure ratio is variable

Mass flow range Mass flow range

Q = M × Hvap

Q – Heat Load; M – Mass Flow Rate; Hvap – Heat of Vaporization

“Cold” cycle (THe = 2.0 K):

M/Mdesign = 75% … 100% Q/Qdesign = 75% … 100% “Hybrid” cycle (THe = 2.0 K): M/Mdesign = 50% … 100% Q/Qdesign = 50% … 100%

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THe = 1.92 K psuc = 2450 Pa THe = 2.0 K psuc = 3130 Pa

Temperature Level Adjusting Capability

THe = 1.96 K psuc = 2780 Pa

“Cold” cycle: “Hybrid” cycle:

THe = 2.0 K psuc = 3130 Pa THe = 1.8 K psuc = 1640 Pa THe = 1.9 K psuc = 2300 Pa supporting 1.8 K … 2.0 K temperature levels 1.9 K temperature level cannot be achieved

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“Cold” cycle

  • Using only cold

compressors

  • Easier to operate
  • Limited capability

– Single temperature level – Limited heat load range

  • Requires use of resistive

heating for operation in

  • ff-design mode

“Hybrid” cycle

  • High dynamic range

– Various temperature levels – Various heat load

  • High efficiency in off-

design mode without resistive heating

  • Using volumetric machine
  • Complex control system

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Conclusions

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Goals & Perspectives

 Develop cold compressor units control system strategy.  Develop common control system strategy including cold compressor units and warm vacuum pump.  Optimize control system strategy.  Compare characteristics of cold and hybrid cycles using models of compression process.  Develop static and dynamic models of coldbox including cold compressors, warm vacuum pump, heat exchangers and another equipment.  Write a technical note.

9 Development of a low-pressure helium compression control strategy for CMTF