1 improvement of compatibility of liquid metals li and pb-17li masatoshi kondo, minoru takahashi b),...
TRANSCRIPT
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Improvement of compatibility of liquid metals Li and Pb-17LI
Masatoshi KONDO, Minoru TAKAHASHI b), Teruya TANAKAa), Tsisar Valentyn c) and Takeo MUROGA a)
Tokai university, Japan, a)National Institute for Fusion Science a) b) Tokyo Institute of Technology, Japanc) Physico-Mechanical Institute of National Academy of Sciences of Ukraine, Ukraine
ISLA2011
2
Background -1Fusion blanket
KOREA HCML-TBM (2008)Li/RAFMDr.KIM et alJapan (2003)
molten salt Flibe/RAFM Dr.Sagara et al., FED
India TBM (2009)Pb-LI ・ solid breeder/RAFM Dr.Kumar et al FED
Liquid breeder Structure
Lithium Li
Lead lithium Pb-17Li
Flibe LiF-BeF2
Vanadium alloy
S i C
ODS
Japan
JapanRussia
Korea
USARAFM
EuropeIndiachina
Toward high temperature
Pure metal
Molten salt
Alloy
Coating(MHD, Ttritum .etc)
Al2O3
Er2O3(DiP ・MOCVD )
Nitride treatment
Er2O3(DiP ・MOCVD )
Japan (2003) liquid metal Li/vanadiumDr.Muroga et al., FED
3
Background -2(Structural material)
Corrosion of RAFM steel in liquid metals
Chemical reaction of steel’s base metal (Fe), alloying elements (Cr, W) and carbides with liquid metals
wt% Cr W C Mn Other
Fe
JLF -1
9 1.94
0.09
0.49
V: 0.2
balance
Chemical composition (wt%)
Reduced activation ferritic martensitic steel is candidate structural material of blanket.
1 0 µm
Prior austenite grain boundary
Packet boundary
Lathboundary
Somesub grains
Blockboundary
4
Background -3 (Liquid breeders)
M.P.
(K)
Thermal conductivity
(W / (m x K))
Density
(kg/m3)
Viscosity
(mPas)
Li Alkali metal 453.7 53.7 (800K) 481 (800K) 0.344 (800K)
Pb-17Li Heavy metal 508 9568 (800K) -
Flinak
(LiF-NaF-KF)
Molten salt 727 1.2 2146 (800K) 4.1 (900K)
Flibe
(LiF-BeF2)
Molten salt 732 1.2 1993 (800K) 7.5 (800K)
FlinakLiquid Lithium
Li+
Free electron
High thermal conductivity in liquid metal High chemical stability of molten salt
Li+ F-+
Already stable state by ion bonding
Major characteristics of liquid breeders
5
Purpose
Purpose of the present study is follows;
- Establish corrosion test technology for liquid Li and Pb-Li
- Make clear the corrosion characteristics of RAFM JLF-1 steel in the liquid metals
- Make clear the corrosion of coating in the liquid metals
- Modeling of the corrosion of RAFM steel in the liquid metals
6
Experimental procedure (1)
Fe Cr W Ni
Li 0.85 0.12 0.31 0.8 Nitrogen: 65
Pb-17Li 2.2 0.17 0.52 1.3 -
Pb-17Li provided by santoku coop.
Temperature 600ºC Time(hours) Re for mixing - Material
LiStatic 30-250-750
High purity, Li3N dopeLi2O dope, C dope
JLF-1Er2O3 coat
Flowing 250 2859 High purity JLF-1
Pb-17LiStatic 250-3000 High purity
JLF-1Er2O3 coat
Flowing 250 18512 High purity JLF-1
Initial impurity of liquid metals (wppm)
Experimental condition
Carbon Li2O Li3N
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Experimental procedure (2)
Influence of flow
3cc
100cc
Fixed specimen
Width of impeller 33 mRotation speed 100 rpmVelocity around specimen v=π dn =0.17cmRe number for mixing
2nd
=Re
48mm
Static test(Simple immersion)
Flowing test(Mixing vessel)
(c) Impurity analysis of liquid breeders by ICP-MS ( Fe, Cr, W, non metal impurity)(To investigate mass balance between loss in specimen and increase of metal impurity in melt )
(b)SEM/EDX analysis for surface and cross section(To evaluate the metallurgical change of steels)
(a) Weight loss measurement(To estimate the corrosion (loss) rate)
Analysis of corroded specimen
Take out sample Li immersion
at 350ºCAcetone
Immersion to ethanol
Acetone
Immersion to ethanol
Cleaning procedure for tested specimen
Specimen in Li
Specimen inPb-Li
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Experimental results (Mass loss of specimen by corrosion in Li)
- The influence of non-metal impurity (i.e. nitrogen and oxygen) in liquid Li was large on the corrosion loss.
- The Influence of oxygen in Li on the corrosion was newly found.)
-2
0
2
4
6
8
10
12
14
Li(+0.8wt%Li2O)
(Static)750-hour
Li(+0.5wt%Li3N)
(Static)250-hour
Li(Pure)(Static)
250-hour
Li(Pure) (Flow)
250-hour
Li(+3.7wt%C)
(Static)250-hour
Wei
ght
loss
of
spec
imen
s (g
/m2 )
Experimental results (Lithium)
20 hour 120 hour 250 hour
Li +0.5wt%Li3N nitrogen dope (Cr dissplution)
1 0 µm 20µm 20µm
選択的
250 hour
Phase transformation
BCTa a
c
a a
a
BCC
C Fe
Phase transformation
Initial
122 hour 780 hour287 hour
Li +0.8wt%Li2O oxygen dope (Cr dissolution)
Li +3.7wt% C carbon dope
1 0 µm 1 0 µm 1 0 µm
Phase transformation
No phase change
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0
20
40
60
80
100
0 10 20 30Er
conc
entr
atio
n in
Li
uni
t: w
ppm
(IC
P-M
S)
0 10 20 30 exposure (hour)
600ºCEr2O3/JLF-1
Surface color was black after the corrosion test though the color was metallic luster before the test.
20 µm
normal
Corroded(Er-Cr rich)
Peeling off
SEM
Crack
-0.10
0.10.20.30.40.50.60.70.80.9
0 50 100 150 200 250Th
erm
al l
inea
r ex
pan
sio
n %
Temperature (ºC)
Li
JLF-1
Er2O3
Corrosion of Er2O3 coating in Li
The oxide itself might be chemically stable in the liquid breeders. The damage was possibly made by a large difference of the thermal expansion ratio between adhered Li and the coating during a heat up and a cool down procedure of the corrosion test when the Li was solidified.
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Summery for corrosion in Li
- Nitrogen dissolved in Li has big influence on the compatibility. It was newly found that oxygen in Li can increase the corrosion of steel. The nitrogen and oxygen dissolved as non-metal impurity in Li must be removed before the use. Carbon in Li can suppress the the depletion of carbon in the steel.
- The issue for the coating of liquid blanket is the peeling of the coatings in the liquid metals.
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Experimental results (Weight loss of specimen in Pb-Li at static condition)
Corrosion was suppressed when the metal element, i.e. Fe and Cr, in Pb-17Li was saturated..
Experimental results (Pb-17Li)
600oC 750 hours
High mag. (x3000)
20µm
5µm
Low mag. (x1000)
600oC 3000 hours
20µm
5µm
High mag. (x3000)
Low mag. (x1000)
The corrosion in JLF-1 was selective attack to some boundaries of microstructure.
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Experimental results (Corrosion of Er2O3 coating in Pb-Li)
20µm20µm20µm
Er
Fe
CrCou
nt n
umbe
r
Resin Pb-Li Steel matrix
0 20 40 60 80
Depth (µm)
The oxide itself might be chemically stable in the Pb-Li. The damage of the coating was possibly made by a large difference of the thermal expansion ratio between adhered Pb-Li and the coating during a heat up and a cool down procedure of the corrosion test when the Pb-Li was solidified.
0
0.2
0.4
0.6
0.8
1
1.2
0 200 400 600Temperature (ºC)
Th
em
al l
ine
ar
exp
an
sio
n (
%)
Li
Pb
JLF-1
Er2O3
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Flowing Li
Internal diffusion of liquid metals
(FAC) (Erosion corrosion)
10µm
Erosion- corrosion was caused by peeling of subgrains after corrosion on surface.
Flowing Pb-17Li
10µm
Experimental results (Corrosion in flowing Li and Pb-Li)
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Corrosion modeling
Li (65wppm nitrogen) Pb-17Li Pb
Solubility(Cs)
wppmMolppm
Fe - * 47 (600ºC) ~<145> 34 (600ºC) <126>
Cr52.4 (800 ºC) <7>~94.3 (600ºC) <12.6>
10 (500ºC) <40> 1 (600ºC) <3.7 >
))V
hStexp(ρVCs(1Δm
C)-(CshJdt
dC
S
Vρ
))V
hStexp(Cs(1C
Transient of metal impurity in liquid breeders
Corrosion ratio
Mass loss of specimen by corrosion
Concentration of metal in liquid breeders
Mass balance between increase of metal impurity in liquid breeders and corrosion ratio of specimen
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Mass transfer model in corrosion (Li)
0
0.25
0.5
0.75
1
1.25
1.5
1.75
2
0 100 200 300 400 500 600 700 800
Wei
ght
loss
per
uni
t are
a (g
/m2 )
Exposure time (hours)
Test A
Test B
Test C
Test D
Different corrosion device
600oC (Li)
Different geometrical factor of corrosion systemVolume / corrosion surface area
V/S
Large
Small
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600oC (Pb-Li)
Mass transfer model in corrosion (Pb- Li)
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Summery
Major conclusions are follows;
- Corrosion test technology for liquid Li and Pb-Li was established.
- The corrosion characteristics of JLF-1 in static Li and Pb-Li were investigated. Then, we started to study about the corrosion in flowing condition.
-Modeling of corrosion of JLF-1 in Li and Pb-Li was started.
- Fundamental corrosion characteristics of anti corrosion coating in liquid Li and Pb-Li was studied. The issue is the peeling off of the coatings in liquid metals.
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22
Corrosion of Fe-Al coating in liquid Pb-Li
10µm
Fe-Al coating
剥離 316LPb-Li
Pb
O
Fe
Al
SEM After 500- hour immersion in Pb-17Li at 600 degree C
Coating it self was chemically stable in liquid Pb-Li.
However, the peeling off is issues for the coating.
Now, study on metal plating technology is under going.
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Background -4Corrosion phenomena
Solubility of metal elements and chemical potential of non- metal impurity in liquid metals are important parameters which determine the corrosion.23
Compatibility
Liquid metal corrosion
Formation of corrosion products
(Carbides, oxides, nitrides, hydrides and so on)
-Dissolution of steel element into liquid metals-Diffusion of metal elements of liquid metal into steel matrix
Determined by alloying process
Determined by chemical potential of non-metal impurity
All liquid metals especially heavy liquid metal
Pb, Pb-Bi
Li, Na, K, Pb-Li(?)
GB attack Erosion- corrosion
Peering of corrosion products
FAC
At flowing condition
At flowing static condition
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0.0001
0.01
1
100
10000
700 800 900 1000 1100 1200 1300
Sol
ubili
ty o
f F
e an
d C
r in
Lith
ium
(w
ppm
)
Temperature of Lithium (K)
Cr in Li (Nitrogen 150wppm)[12]
Solubility of Cr in Li (Nitrogen <10wppm) [11 ]
Solubility of Fe in Li (Nitrogen 500wppm)[11]
Solubility of Cr in Li (Nitrogen 200wppm) [11]
Solubility of Fe in Li (Nitrogen <10wppm) [11 ]
Solubility Cr in Li (Nitrogen 790wppm)[12 ]
Solubility of Cr in Li (Nitrogen 65wppm) used in present study
3LiFeNLiFeN2Li 233 3LiCrNLiCrN5Li 593
Effect of nitrogen on corrosion in Li
25
Experimental results (Transient of metal impurity in Pb-17Li)
0
2
4
6
8
10
12
0 500 1000 1500 2000 2500 3000 3500
FeCrWMn
Time (hours)
Con
cent
ratio
n (w
ppm
)
[1] M. G. Barker, P. Hubberstey, A. T. Dadd, S. A. Frankham, J. Nucl Mater., 114, 143-149 (1983). [2]V. Tsisar, M. Kondo, et al., J. Nucl. Mater, under review. H. U. Borgstedt, H. Feuerstein, J. Nucl. Mater., 191-194, 988-991. [3]N. Simon et al., Int. J. Heat Mass Transfer., vol.38, No.16, 3085-3090 (1995).
After the immersion of JLF-1 in Pb-Li.