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Techniques for analysis and purification of nitrogen and argon

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IDEA Meeting, MPI-K Heidelberg, 21-22.October 2004 ... Cosmogenic. 39Ar. 1.4 Bq/m3 air. 1.2 MBq/m3 Kr. 235U fission (nuclear fuel reprocessing plants) ... – PowerPoint PPT presentation

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Title: Techniques for analysis and purification of nitrogen and argon


1
Techniques for analysis and purification of
nitrogen and argon
  • Grzegorz Zuzel
  • MPI-K Heidelberg

2
Outline
  • Motivation of this research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

3
Motivation
  • Ultra-pure LN2/LAr will be used by the GERDA
    experiment
  • - Cooling medium for naked Ge crystals
  • - Shield against external radiation
  • Developed techniques could be applied in other
    low-level experiments

4
Outline
  • Motivation of the research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

5
Production of N2 and Ar
  • N2 and Ar are produced from air by rectification
  • Traces of atmospheric noble gases remain in final
    product
  • Final purity depends on individual plant and
    handling

6
Outline
  • Motivation of the research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

7
Radioactive noble gases in the atmosphere
8
Requirements for GERDA
  • 222Rn
  • MC simulations Bernhard Schwingenheuer
  • 0.3 µBq/m3 N2 (STP) 10-4 evt/(kg?y?keV)
  • 42Ar
  • MC simulations Stefan Schönert
  • 50 µBq/m3 Ar (STP) 4?10-5 events/(kg?y?keV)
  • 42Ar naturally low enough

9
Requirements for GERDA
  • Q-value of 39Ar and 85Kr below 700 keV
  • But dead-time problem when Ar scintillation is
    used (slow decay time1µs)
  • Assume 10 m3 active volume
  • 39Ar rate 17 kHz OK!
  • 85Kr rate not higher ? 0.3 ppm krypton

    required
  • In case of LN2 and dark matter detection
    39Ar lt 2.4 µBq/m3 N2 (0.2 ppm Ar in N2)

    85Kr lt 1 µBq/m3 N2 (1 ppt Kr in
    N2)

10
Outline
  • Motivation of the research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

11
Low-level proportional counters
12
Low-level proportional counters
  • Developed for the GALLEX experiment
  • Can be applied for a- and ß-detection
  • Handmade at MPI-K (ultra-pure quartz)
  • Background 1 cpd for E gt 0.5 keV
  • Active volume of about 1 cm3
  • Special filling procedure is required

13
Counter filling line
14
Sensitivities
  • 222Rn - only a-decays detected




    - 50 keV threshold (bkg 0.2 2 cpd) - total
    detection efficiency 1.5 ? abs.
    detection limit 30 µBq (15 atoms)
  • 39Ar and 85Kr - ß-decays detected
    - 0.6 keV threshold (bkg 1-5
    cpd) - total det. efficiency 0.5 ?
    abs. det. limit 100 µBq (5x104
    85Kr atoms)

15
Measurements of 222Rn in gases MoREx (Mobile
Radon Extraction Unit)
16
Measurements of 222Rn in gases MoREx (Mobile
Radon Extraction Unit)
222Rn detection limit 0.3 µBq/m3
17
Ar and Kr mass spectrometry
18
Ar and Kr mass spectrometry
  • Devoted to investigate rare gases in terrestial
    and extraterrestial samples
  • Coupled with the sample preparation and
    purification sections (cryo- and getter pumps)
  • System operated at ultra-high vacuum (10-10 mbar)
  • Sample size typically 1cm3
  • Detection limits
    Ar 10-9 cm3 (1 ppb 1.4 nBq/m3 for 39Ar
    in N2) Kr 10-13 cm3 (0.1 ppt 0.1
    µBq/m3 for 85Kr in N2)

19
Outline
  • Motivation of the research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

20
Different possibilities
  • Distillation
    - high costs and energy
    consumption
  • Sparging (e.g. with He)
    - boiling point for contaminants must
    be lower than for the gas to
    be purified
  • Adsorption -
    successfully used for 222Rn removal from nitrogen
    - a lot of
    experience at MPI-K

21
Gas purification by adsorption
  • Applied when high purities are required
  • Based on differences in binding energies
  • Strong dependence on temperature
  • Activated carbons and zeolites are widely used as
    adsorbers

22
Henrys law
n H ? p
  • n number of moles adsorbed mol/kg
  • p partial pressure of adsorptive Pa
  • H Henry constant mol/(kgPa)
  • H determines the retention volume

VRet H?R?T?mAds
23
Purification in the column
24
Single component adsorption model
  • Prediction of Henry constant for adsorption on
    activated carbon
  • Only one parameter is involved TCpC-0.5
  • Allows to compare adsorption of different
    components
  • S. Maurer, Ph.D. thesis, TU Munich (2000)

25
Single component adsorption model
26
Purification of N2/LN2 from 222Rn
  • Strong binding to almost all adsorbers
  • Easy trapping with activated carbon at 77 K
  • Problem 222Rn emanation due to 226Ra
  • Requires careful material selection
  • Activated carbon CarboAct
  • 222Rn emanation rate (0.3 ? 0.1) mBq/kg
  • 100 times lower than other carbons

27
Purification of N2/LN2 from Kr
  • Single component adsorption model fails for
    binary system N2/Kr
  • More advanced models predict strong dependence of
    H on the pore size of the adsorber and its
    internal polarity
  • Henry coefficient expected to be higher for pure
    gas phase adsorption (at T gt 77 (87) K for N2
    (Ar))
  • Cooling LAr (for N2) or pressurized liquid
    gases
  • Pores, low polarity and adsorption from gas phase
    should lead to H 1 mol/kg/Pa

28
Henry constant and pore size
29
Considered adsorbers
  • Hydrophobic zeolite MFI-type low internal
    polarity, pores 5.3 Å
  • Hydrophobic zeolite BEA-type a bit larger
    polarity than for MFI, pores 6.6 Å
  • Carbo Act F3/F4 low 222Rn emanation rate, wide
    pore size distribution
  • Charcoal Cloth FM 1-250, fabric
  • Activated Carbon C38/2, optimized for solvent
    recovery

30
Experimental setup
31
Purification of N2 Summary
  • 222Rn removal rather easy, even from LN2
  • Ar removal impossible
  • Kr removal requires
  • Low temperature gas phase adsorption
  • Pore size-tuned adsorbers with low internal
    polarity
  • Low 222Rn emanation rate

32
Single component adsorption model
33
Purification of Ar
  • (Almost) no difference between Ar and N2 for
    adsorption on activated carbon
  • However higher temperatures have to be considered
  • 222Rn removal should not be a problem
  • Kr removal from Ar even more challenging than for
    N2 (especially for large amounts)

34
Outline
  • Motivation of the research
  • Production of N2 and Ar
  • Radioactive noble gases in the atmosphere
  • Methods of analysis
  • Purification of N2 and Ar
  • Conclusions and planned activity

35
Conclusions and planned activity
  • Techniques for measuring ultra-low radioactivity
    levels available _at_ MPI-K
  • Nitrogen purification intensively studied
  • - Adsorbers selection based on the
    adsorption theory
  • - Experimental tests are ongoing
  • - Purity tests for different supply
    chains are planned
  • Argon purification seems to be a very similar
    problem
  • Purity and purification tests for Ar recently
    started
  • Although the program was slightly extended it is
    progressing as scheduled
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