a demonstrator of a pav for tritium recovery from …3 rationale of developments of pav iea...
TRANSCRIPT
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A demonstrator of a PAV for tritium
recovery from LLE at HCLL TBM
loop operational ranges
Ismael Martínez, B. Herrazti, G. Veredas, J. Fradera,
I. Fernández, L. Batet, I. Peñalva, L. Mesquida,
J. Abellà, J. Sempere, L. A. Sedano
IEA International Workshop on Liquid Metal Breeder Blankets, 23-24 September, 2010 (Madrid), Spain.
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Summary
• Rationale of development of a Permeator Against
Vacuum (PAV) as Tritium recovery Technology (in
front of: gas-liquid contactors, bubblers and getters)
• Optimized design option for PAV [Fuskite®]
• Fuskite ®: Numeric efficiency assessment
• Experimental lay-out of an in-prototype
demonstration project
• Conclusions
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
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Rationale of developments of PAV
IEA International Workshop on Liquid Metal Breeder Blankets, 23-24 September, 2010 (Madrid), Spain.
• Tritium (T) supply for DEMO is a serious concern after ITER
(27kg available in the second decade of XXI century and
ITER consumption is about ~15kg)
• External production of T is known as non economical (In
Fusion we should produce our own T). Reliable breeding
blanket technology is a must.
• At present plasma low T burn-up scenarios Fuel self-
sufficiency depends strongly on T residence time in Plant
Systems
• Considering present T residence times in ITER Plant
Systems (hours) [TRIMO modelling], the design of T plant for
DEMO is expected to differ strongly from that of ITER.
• T residence time in blanket systems and T recovery times in
T Extraction Systems (TES) should be comparable to T
residence time in Plant Systems.
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)()1()(0 PRRPR tt
b
cbt
b
cttHI
)()( PRPRP ttcTBRt
b
cttH
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
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Tritium extraction techniques
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
TES Technique tR Weaknesses
PB Sweepers +
TRS (CTs, MSBs,
getters)
Hours •Low efficiency, large systems
•Parallel batch systems (TRS)Dynamic
inventories
•Sizing at DEMO scale (TRS)
•Power consumption
PB Strippers
+TRS (CTs, MSBs,
getters)
Hours •Injectors for sub-mm bubbles
•Size of Packed Beds
•Parallel batch systems (TRS)
•Sizing at DEMO scale
•Power consumption
Inmersed getters Hours •Poor and non validated database for
breakthrough
•Parallel batch systems
Inmersed PAV Tens of seconds •In-prototype demonstration pending
TRS: Tritium Recovery System
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• Conceptually minimizes the T recovery time in blanket systems
• Tritium can be directly transferred to fueling systems in T-plant (minimum purification requirements and direct re-fueling)
• High potential efficiency and compactness by design
– High contact surface by geometrical design
– Optimized hydrodynamics for LLE (channels)
– Materials with a high Ks factor (a-Fe, steel or Nb)
• Simple/natural integration in a piping loop system
– Huge space and weight savings
• Easy manufacturing low cost
• Passive
– Only a vacuum pump is needed
– Efficiency can be thermally driven
• Potentially T breeding and recovery systems inside Bioshield (safety! & also environmental impact)
Strengths of Permeators Against Vacuum for TES
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
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)),,,(exp(1)( * LzhRvAL m
FeS
LiPbS
T
m
m
K
K
D
zh
vR
h
A
,
,
*
1
2
PAV conceptual efficiency
mh Re,Sc
HydrodynamicsWe need turbulent flow
TS DK , chemistry
Rz, geometry
Higher A and L is
better
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
L
How would it be the most compact and efficient permeator?
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Towards a highly efficient and
compact PAV
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
FUSKITE ®
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• Assuming steady-state, the microscopic
mass balance in a differential radial volume
of the membrane is, and the boundary
conditions:
• After integration the concentration profile is
found.
• The molar flux through the membrane wall
facing the LM can be expressed as follows
• and the molar rate reads,
• With the continuity conditions
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
PAV concept: numerical qualification
01
dr
dCr
dr
d
r
)()(
)()(
22
11
rCrCrr
rCrCrr
)/ln(
)/ln(
)()(
)()(
21
2
21
2
rr
rr
rCrC
rCrC
dr
dCDJ T
dr
dCrLDS T2
LMsSMTSMsLMT kCkC ,,,,
• The overall mass transfer coefficient (kt) is
computed from that in the boundary layer
(hm) and transfer from the bulk in LL
• Therefore:
)/ln(
)()(
221
2
,
,
1
rr
rCk
krC
LDSSMTs
LMTs
T
TmT LD
rr
hk 2
)/ln(11 21
Tm
SMTs
LMTs
T
LD
rr
h
rCk
krC
LDS
2
)/ln(1
)()(
221
2
,
,
1
dDSch Tm /Re0096.0 346.0913.0
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PAV concept: numerical qualification• A simplified axis-symmetric 3D domain is
needed in order to save computational time.
• Due to the spiral cross section, the domain
is represented by a sector consisting of
series of concentric annular channels.
• Two cases assessed:
– inlet v of 1 mm/s (laminar case)
– Inlet v of 10cm/s (turbulent case)
a channel height of 5mm and a tube length
of 2m. In the present work a 2m long
permeator with 45 concentric channels
Membrane thickness is set to 1mm with a
vacuum space of 1mm.
Channels are 5mm thick.
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PAV concept: numerical qualification
• DEMO HCLL
– Low velocity ~1mm/s
– Laminar regime hm=10-5 m/s,
Re=65
– High efficiency at small
diameters
– Very compact
– Surface rugosity not optimized
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
• DEMO DCLL
– High velocity ~ tens of cm/s
– Turbulent regime hm ~ 10-3 m/s,
Re>500
– High efficiency at medium
diameters
– Surface rugosity not optimized
HCLL
DCLL
• In the present work a k- SST for low
Reynolds numbers has been used (see
Gordeev et al. )
• TMBF (Lefhalm et al.) give better results
for LM (Carteciano et al.)
• Laminar solver does not reach the steady
state, but an oscillatory regime. On the
contrary, turbulent solver reaches the
steady state.
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PAV demonstrator prototyping
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
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PAV demonstrator prototyping
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
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Conclusions
• PAV appears as the most simple, economical, system
integrable and reliable TES solution for ITER and
DEMO LM blankets
• A PAV optimized design (Fuskite ®) has been
proposed: potentially for ITER and DEMO
• Numerical efficiency qualification anticipates
promising performances
• Prototype demonstrator is under construction
IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
15IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
16IEA International Workshop on Liquid Metal Breeder Blanket, 23-24 September, 2010 (Madrid), Spain.
Thank you!!!! Gracias!!!!