implementation concepts for unattended measurement systems at enrichment plants
DESCRIPTION
Implementation Concepts for Unattended Measurement Systems at Enrichment Plants. L. Eric Smith, Alain Lebrun IAEA January 2012. IAEA’s “Model Approach for GCEPs”. High-capacity plants pose implementation challenges for c urrent approaches. . Safeguards objectives: Timely detection of… - PowerPoint PPT PresentationTRANSCRIPT
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IAEAInternational Atomic Energy Agency
Implementation Concepts for Unattended Measurement Systems at
Enrichment Plants
L. Eric Smith, Alain LebrunIAEA
January 2012
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IAEA
Safeguards objectives: Timely detection of…• Diversion from declared input and output • Undeclared (excess) production of normal enrichment levels• Higher-than-declared enrichment (e.g. HEU)
Implementation objectives• Reduce need for routine measurements, sampling during inspections*• Ease and expedite cylinder release process for facility operators
IAEA’s “Model Approach for GCEPs”
How might unattended measurement systems contribute?
*Related work by Boyer, et al. (IAEA Symposium 2010)
High-capacity plants pose implementation challenges for current approaches.
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IAEA
Potential Roles: Unattended Measurement Systems
Storage MBA
Load-cell monitoringOnline Enrichment Monitor
(OLEM)M(t) for each cylinderHigh-accuracy E(t) for each
cylinderContinuous gas monitoring
Ecyl = E(t)*M(t)
Process MBA
Unattended Cyl. Verification Station (UCVS)
High-accuracy net mass“NDA Seal” for CoK on cylinder
contentsAssay of blended cylindersMU
M235 = Ecyl * MU
NaI(Tl)
UF6
Collimator
E(t)
Pressure (Temp)
mComputer
Pressure
Load Cell
Cylinder
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IAEA
Concept: Load-Cell Monitoring
tstart tendM(t)
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IAEA
Concept: On-Line Enrichment Monitor
P ~ 4 Torr
E(t) ∝ Rgas_186keV (t) * rgas (P, T, t)
NaI(Tl)
CEMO
Header Pump
1) High-accuracy E(t) for product and tails
2) Continuous monitoring of gas
Cascade 1
Cascade 2
Cascade 3
Cascade 4
P ~ 40 Torr
Gas Sampling
Load Cell
UF6
Header Pipe
PressureTemperatu
re
Mass Spec Analysis
CylinderOLEM
M(t)
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OLEM Viability Studies: Examples
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
9.0
10.0
Tota
l Unc
erta
inty
(%)
.
Product
Feed
Tails
E = 5.0%Low P High PHigh D Low D
E = 2.0%Low P High PHigh D Low D
E = 0.711%Low P High PHigh D Low D
E = 0.2%Low P High PHigh D Low D
Low P: 10 TorrHigh P: 50 TorrLow D: 100 mg/cm2
High D: 1000 mg/cm2
Statistical uncertainty only--systematic uncertainties are not addressed.**
**Plot from Smith and Lebrun (IEEE Nuclear Science Symposium, 2011)Related work by Ianakiev (ESARDA 2010) and March-Leuba (personal
communication, 2012)
Performance Targets
Tails: sT < 3%
Feed: sF < 2%
Product: sP < 1%
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Concept: Unattended Cylinder Verification Station
Mass: Shared-use or IAEA scale
NDA**: Hybrid (PNNL), PNEM (LANL), other?
Cylinder ID: L2IS, Global Bar Code, other?
Surveillance: NGSS
**from Smith (INMM 2010)
1) Apply and verify “NDA Seal” at MBA boundaries (CoK)
2) Unattended NDA of M235 for blended cylinders3) Recovery of CoK on cylinders4) Platform for weight, NDA verification during
inspections
**Related WorkSmith (IEEE TNS 2010, INMM 2010), McDonald (INMM
2011)Miller (ESARDA 2011)
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UCVS Viability Studies: Example“Hybrid NDA” for 235U Assay (30B cylinders)
8
sP = 2.5%
**Plot from Smith et al. (INMM 2010)
Intl. Target Value: sP ~ 5%
Hybrid NDA (preliminary)sP ~ 2.5%sF ~ ??sT ~ ??
Other NDA methods?
NDA Seal?
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“Special” treatment of feed• Challenges
• Largest 235U flow rate• Poor assay accuracy (OLEM wall-deposit issues, UCVS > 6%)
• Advantages (assuming natural feed)• Isotopics are precisely known• Cylinders should be homogeneous
Baseline Concept• No quantitative assay of feed assume Ecyl = 0.711% sF ~ 0.0%...if• UCVS verifies that Ecyl_UCVS is consistent with feed-cylinder profile• OLEM only on product and tails header pipes• UCVS quantitative NDA on blended product cylinders
UMS Implementation Concepts
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IAEA
Scenario: Diversion into MUF or D• 235U bias defect in product and tail cylinders• SQ = 75 kg 235U (LEU, NU, DU)
Viability Metric: Fidelity of 235U mass balance (“IMUF”)• Assume no waste, scrap, etc. • IMUF = F – (P + T) • sMUF
2 = sF2 + sP
2 + sT2
• Threshold = 3*sMUF
• PD for 1SQ diversion?
Implementation Concepts: Viability AnalysisOverview
**from C. Norman, IAEA
PD
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Implementation Concepts: Viability Analysis
kg U/year cylinders/yearFeed Product Tails Feed Product Tails
6 000 000 1 000 000 5 000 000 710 667 592
Reference Facility: 4,000,000 SWU/year, 0.711%, 3.0%, 0.25%
Analysis variables: OLEM s , UCVS sP , blend fraction, balance period
Balance Period = 1 month = Baseline ConceptConcept UCVS s Blend s (SQ) PD (%)
ID Fraction F T Total TotalF P T P OLEM UCVS
1 0.0 1.0 3.0 3.0 0.05 0.00 0.32 0.05 0.42 0.53 13.62 0.0 0.5 1.5 3.0 0.05 0.00 0.16 0.05 0.21 0.27 77.43 0.0 1.0 3.0 3.0 0.30 0.00 0.23 0.30 0.42 0.56 11.04 0.0 1.0 3.0 6.0 0.30 0.00 0.23 0.60 0.42 0.77 4.55 2.00 1.0 3.0 0.0 0.00 0.95 0.33 0.00 0.42 1.09 1.9
s (SQ)P
OLEM s
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Implementation Concepts: Viability Analysis
Balance Period = 1 week
Concept UCVS s Blend s (SQ) PD (%)ID Fraction F T Total Total
F P T P OLEM UCVS1 0.0 1.0 3.0 3.0 0.05 0.00 0.07 0.01 0.10 0.12 100.02 0.0 0.5 1.5 3.0 0.05 0.00 0.04 0.01 0.05 0.06 100.03 0.0 1.0 3.0 3.0 0.30 0.00 0.05 0.07 0.10 0.13 100.04 0.0 1.0 3.0 6.0 0.30 0.00 0.05 0.14 0.10 0.18 99.65 2.00 1.0 3.0 0.0 0.00 0.22 0.08 0.00 0.10 0.25 83.7
s (SQ)P
OLEM s
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IAEA
• High-capacity plants require new instruments and approaches
• Integrated UMS: “Independent” 235U and U balances on 100% flow • NDA Seal for cylinder CoK• Special treatment of feed• PD values (scoping) for protracted diversion are encouraging
• UMS Role: Rule out protracted diversion between inspections• Machines do routine measurements• Inspectors do what humans do best (investigate)
• Many questions and issues ahead…for example• Relevance for diversion and excess production scenarios• Realistic OLEM and UCVS uncertainties• Data security for shared-use instruments• Operator impacts, acceptability
Conclusions
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Additional Information
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Potential Impacts to Operators
Potential ImpactEased and expedited cylinder release processReduced physical presence of inspectorsReduced sampling requirements on cylindersCylinder tracking infrastructureOLEM for process control and criticality controlLoad-cell (and accountancy scale?) data sharingOLEM nodes installed on header pipes (2 per unit); additional P gaugesUCVS installation(s)UCVS scans on cylinders moving in/out of MBAs
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Material Flow and Data Streams
Load Cell: M(t)OLEM: E(t) Ecyl_OLEM = E(t)*M(t)Ecyl_OLEM : sP < 1%, sT <
3%
Process MBA
NDA SealScale: Mempty , Mfull , sM <
0.1% M235_OLEM = Ecyl_OLEM * MU
M235_OLEM : sP < 1%, sT < 3%
OLEM
Load Cell
UCVS Storage MBA
Facility-Level Data: MU , M235_OLEM , NDA Seal
Unblended Product and Tails Cylinders
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Material Flow and Data Streams
Load Cell: M(t)Ecyl = known = 0.711%Ecyl : sF ~ 0.0%
Process MBA
NDA Seal: “nominal” feed?Scale: Mempty , Mfull , sM < 0.1% M235 = Ecyl * MU
M235 : sF ~ 0.1%
Load Cell
UCVS Storage MBA
Facility-Level Data: MU , M235 , NDA Seal
Feed Cylinders
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Material Flow and Data Streams
Process MBA
Quantitative NDA of Ecyl_UCVS : sP ~ 3 - 6%NDA SealScale: Mempty , Mfull , sM < 0.1% M235_UCVS = Ecyl_UCVS * MU
M235_UCVS : sP ~ 3 - 6%
Blending Station
UCVS Storage MBA
Facility-Level Data: MU , M235_UCVS , NDA Seal
Blended Product Cylinders
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Implementation Concepts: Viability Analysis
Balance Period = 2 weeks
Concept UCVS s Blend s (SQ) PD (%)ID Fraction F T Total Total
F P T P OLEM UCVS1 0.0 1.0 3.0 3.0 0.05 0.00 0.15 0.02 0.19 0.24 86.92 0.0 0.5 1.5 3.0 0.05 0.00 0.07 0.02 0.10 0.12 100.03 0.0 1.0 3.0 3.0 0.30 0.00 0.11 0.14 0.19 0.26 80.04 0.0 1.0 3.0 6.0 0.30 0.00 0.11 0.28 0.19 0.35 43.15 2.00 1.0 3.0 0.0 0.00 0.44 0.15 0.00 0.19 0.50 15.7
s (SQ)P
OLEM s
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IAEA
• Quantitative assay of cylinder enrichment M235 in each cylinder• Measurement scenario: Single measurement of many different cylinders • Key metric: Absolute accuracy for quantification of M235• Preliminary accuracy targets: sP < 3%, sF < 6%, sT < 9% for M235• Full-volume interrogation (i.e. sensitive partial defect detection)• Unattended operation
• NDA Seal Continuity of knowledge on cylinder contents• Measurement scenario: Repeated measurements on a single cylinder• Key metric: Reproducibility of key signatures and attributes • Candidate attributes: E, MU, 234/235, 232/235, 235 spatial distribution• Preliminary uncertainty targets: TBD, but likely < 0.5%• Full-volume interrogation (i.e. sensitive partial defect detection)• Unattended operation
UCVS Technical Objectives
The NDA Seal is a recent addition to the potential roles of the UCVS. The concept requires a viability assessment based on
measurements and modeling.
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“NDA Seal”
Collection of distinguishing signatures and attributes that can be used to provide and
recover CoK of the cylinder contents.
Reproducibility of these attributes is the key metric.
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UCVS: Signatures and Attributes For 235U NDA and NDA Seal
Neutrons from F-19 (a, n) U-234U-234 is primary a emitterNeutron escape: ~0.80 full-volumeIndirect measure of U-235Indicator of feed type
Traditional 186-keV g U-235 concentration in outer UF6Direct measure of U-235, but weakly penetratingArray of spectrometers axial distribution of U-235
Neutron-induced g U-234 Iron as n g converter
Fe-56 + n Fe-57 + g (7.63,7.65 MeV)Indirect neutron detection
2614-keV g U-232 “flag” Presence of U-232 reactor recycle feed
Induced-fission neutrons U-235Direct measure of U-235For thermal interrogating neutrons, only outer layer of UF6
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IAEA
Performance Metrics for Quantitative Assay
23
sNDA2 = sstat
2 + ssys_cal2 + ssys_ran
2
Declared Enrichment (%)
Ass
ay E
nric
hmen
t (%
)
sstat~ ssys_cal
Prediction: ssys_cal > sstat and ssys_ran
~ ssys_ran
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Performance Metrics for NDA Seal
24
sseal2 = sstat
2 + ssys_ran2
Number of Measurements on Same Cylinder
Attr
ibut
e
~ ssys_ran
Prediction: ssys_ran can be small, so must minimize sstat
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OLEM Uncertainty BudgetProduct Material
0.0
0.5
1.0
1.5
2.0
2.5
3.0
Unc
erta
inty
Con
tribu
tion
(%)
.
PressureTemperature186-keV: Deposit186-keV: GasTotal
E = 5.0%P = 10 TorrD = 1000
E = 5.0%P = 50 TorrD = 1000
E = 2.0%P = 50 TorrD = 1000
E = 2.0%P = 10 TorrD = 1000
E = 2.0%P = 10 TorrD = 100
E = 5.0%P = 50 TorrD = 100
E = 2.0%P = 50 TorrD = 100
E = 5.0%P = 10 TorrD = 100
E = wt% 235U for gas, depositP = gas pressure (Torr)D = deposit thickness (mg/cm2)
OLEM target for sE
*From Smith and Lebrun, IEEE Nuclear Science Symposium, 2011