div. of plasma application & tech
DESCRIPTION
H 2 Retention and Physical/Chemical Evaporation Problems from the Interactions between ECR Plasma and FLiNaK Molten Salt. Taihyeop Lho , Yong-Sup Choi, and HyonJae Park. National Fusion Research Institutes, 113 Gwahangno , Yusung-Gu , Daejeon 305-333, Korea. - PowerPoint PPT PresentationTRANSCRIPT
1 Div. Of Plasma Application & Tech.
H2 Retention and Physical/Chemical Evaporation Problems from the Inter-actions between ECR Plasma and FLi-
NaK Molten Salt
National Fusion Research Institutes, 113 Gwahangno, Yusung-Gu, Daejeon 305-333, Korea
Taihyeop Lho, Yong-Sup Choi, and HyonJae Park
PMIF 2011, Julich in Germany / 19 ~21 Sep. 2011
2 CPC : Convergence Plasma research Center
CONTENTS of PRESENTA-TION
Introduction - Objectives Experimental Setup o Plasma Parameters o Magnetic field structure Interaction between the plasma and molten salt (FLiNaK) o Ar plasma o H2 Plasma Hydrogen retention Morphology Future Plan - Research Load Map
3 CPC : Convergence Plasma research Center
INTRODUCTION - OBJECTIVES Molten salts have been suggested as the one of the liquid wall material in a fusion device. The advantages of the liquid wall materials are heat removal, re-freshing wall conditions and more. Molten salts have low thermal conductivity which indicates low
heat transfer to the structure of the device. In addition, molten salts have low electrical conductivity (~102 Ω-1
m-1) which is relatively weak MHD effects on the surface flow comparing to the liquid lithium.
The molten salt also have low chemical reactivity and low evapo-ration. However, we don’t know about the possibility of molten salts as a plasma facing material. This research aims on the feasibility test of the possibility.
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EXPERIMENTAL SET-UPOverall Review on Molten Salt Exp. System
Items Spec.Chamber D=520 mm
H=640 mmB-Field Magnet CoilMagnet Power
100A max 875 G/ 20A
MW Freq. 2.45 GHzMW Power 2kW Max.Turbo sys. 1600 lpsBacking Pump
1000 lpm
Gas Con-trol
MFC, 100 sccm
Gas Ar, H2
Molten Salt Heater
700 oC max 100 pie
FLi-NaK
ECR Source
Process Cham-ber
Pump-ing Sys-tem
Magnetron
Magnet Power
Mag-netron-Power
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EXPERIMENTAL SET-UP
PM Tube
To Pumping Sys-tem
To DAS
To DASThermocou-
ple
Function Gen.
640 mm
Focal Length : 750mmApeture Ratio : f/9.8Grating : 1800 Gr/mmResolution : ~ 0.02 nm
Langmuir Probe : ¼ inch one side planar probe
520 mm
Resonance Layer
150mm
RGA : Stanford Labora-tory
6 CPC : Convergence Plasma research Center
174 mm
221mm25m
m
80 mm
91mm
55mm 20m
m
Molten Salt
Probe position
55mm
20
MAGNETIC FIELD STRUCTURE
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-150 -100 -50 0 50
-0.01
0.00
0.01
0.02
0.03
0.04
0.05
0.06 -8cm -7 -6 -5 -4 -3 -2 -1 0 1 2 3 4 5 6 7 8
I sat[A
]
Vbias
[V]
Cylinderical ProbeD0.25, L12mm
■ Hydrogen Plasma density, Temperature and potential
-10 -8 -6 -4 -2 0 2 4 6 8 10
5
10
15
20
25
Vp Te
Position from center [cm]-10 -8 -6 -4 -2 0 2 4 6 8 10
0.0
1.0m
2.0m
3.0m
4.0m
5.0m
6.0m
7.0m
I sat(@
-100
V)[V
]
Position from center [cm]-10 -8 -6 -4 -2 0 2 4 6 8 10
0
1x1010
2x1010
3x1010
4x1010
5x1010
6x1010
Laframboise plot
N[#
/cm
3 ]
Position from center [cm]
PLASMA PARAMETERS
Cylindrical Langmuir probe : Diameter 0.5 mm, Length 12 mm Unmagnetized plasma assumption : Laframboise Analysis Hygrogen Plasma
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I. Experiment condition Base pressure: 6ⅹ10-6 TorrWorking pressure: 1mTorr, Ar 16 sccmECR head input current: 17AMicrowave input power: 500 wattInitial FLiNaK temp.: 28 ℃
II. Measured by monochromatorMeasuring range: 300~850 nmResolution: 0.275 nm2000 point
300 400 500 600 700 800
7800
8000
8200
8400
8600
8800
9000
9200
9400
Ar
K I696.5
Na I588.99
Em
issi
on in
tens
ity (a
rb.)
Wavelength (nm)
Ar 1mTorr 500watt, 17A
K I404.7
Ar
Interaction between Ar ECR plasma and solid FLiNaK
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Interaction between Ar ECR plasma and Liquid FLiNaK
I. Experiment condition Base pressure: 6ⅹ10-6 TorrWorking pressure: 1mTorr, Ar 16 sccmECR head input current: 17AMicrowave input power: 1000 wattInitial FLiNaK temp.: 539 ℃
II. Measured by monochromatorMeasuring range: 300~850 nmResolution: 0.275 nm2000 point
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Ar plasma interaction with the molten salt Heat load by ions and electrons to the molten salt is about 30kW/m2
MAX
Radial density profile included ΔT ~ 50℃ after plasma load (initial temperature =500 ℃)
Resonance Layer
Molten salt bath
NUMERICAL SIMULATION
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I. Experiment condition
Base pressure: 4.3ⅹ10-6 TorrWorking pressure: 1mTorr, H2 46 sccmECR head input current: 17AMicrowave input power: 500 wattInitial FLiNaK temp.: 15 ℃
II. Measured by monochromator Measuring range: 300~850 nmResolution: 0.275 nm2000point
300 400 500 600 700 800
10000
15000
20000
25000
30000
35000
H656.4H
486.3
Li I610.4
Na I568.8
K I404.7
K I766.6769.9
Li I670.9
Em
issi
on in
tens
ity (a
rb.)
Wavelength (nm)
1mTorr 500watt, 17A
Na I589.3
Interaction between H2 ECR plasma and solid FLiNaK
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I. Experiment condition Base pressure: 3.9ⅹ10-6 TorrWorking pressure: 1mTorr, H2 57 sccmECR head input current: 17AMicrowave input power: 500 wattInitial FLiNaK temp.: 539 ℃
II. Measured by monochromatorMeasuring range: 200~850 nmResolution: 0.2 nm3250 point
200 300 400 500 600 700 800
10000
15000
50000
55000
60000
K I766.6769.9
Li I670.8H
486.1
Na I589.3
Na I568.8
H I434
H 486.1
H I410.4
Na I330.4
Em
issi
on in
tens
ity (a
rb.)
Wavelength (nm)
1mTorr, liquid 500watt, 17A
K I344.8
Interaction between H2 ECR plasma and liquid FLiNaK
685 690 695 700 705 710 715
15000
20000
25000
30000
35000
F I712.7
F I703.7F I
690.2
Em
issi
on in
tens
ity [a
rb.]
Wavelength [nm]
F I685.6
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EDS ANALYSIS - MORPHOLOGY
C-K O-K F-K Na-K K-KBase_pt1 3.22 0.36 37.27 0.96 58.19Base_pt2 1.14 0.92 59.09 9.72 29.13
C-K O-K F-K Na-K K-K
Base(18)_pt1 1.51 0.64 53.05 6.35 38.44
Base(18)_pt2 1.10 61.55 8.26 29.08
Base(18)_pt3 1.79 41.38 4.46 52.37
C-K F-K Na-K K-K4.04 57.4 8.62 29.94
EDS analysis before the interac-tion
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RGA CALIBRATION
39600 39900 40200 40500 40800 41100 41400 41700
-2.0x10-8
-1.5x10-8
-1.0x10-8
-5.0x10-9
0.0
5.0x10-9
1.0x10-8
1.5x10-8
Pres
sure
[Tor
r]
Time [s]
F HF Li Na K
H2 inlet0 500 1000 1500 2000
1E-8
1E-7
1E-6
H2
A
H2
0.0 0.5 1.0 1.5 2.00.0
5.0x10-8
1.0x10-7
1.5x10-7
2.0x10-7
2.5x10-7
3.0x10-7
H2 P
r[Tor
r]
Flow [sccm]
Equation y = a + b*xWeight No WeightinResidual Sum of Squares
9.34314E-17
Adj. R-Square 0.99792Value Standard Erro
B Intercept 2.82072E- 2.43053E-9B Slope 1.25287E- 2.33262E-9
Pr=2.8e-8+1.25e-7*Flow
RGA can detect the elements from the molten salt even though without the plasma interaction.
Need RGA calibration for hydro-gen retention to find the total amount of hydrogen retention.
Time (sec)
H2 P
ress
ure
(Torr)
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25100 25200 25300 25400 25500 25600 25700 25800-2.0x10-8
0.02.0x10-8
4.0x10-8
6.0x10-8
8.0x10-8
1.0x10-7
1.2x10-7
1.4x10-7
1.6x10-7
1.8x10-7
2.0x10-7
Pres
sure
[Tor
r]
Time [s]
F HF Li Na K
Plasma interaction region
17400 17600 17800 18000 18200 18400 18600 18800-2.0x10-8
0.0
2.0x10-8
4.0x10-8
6.0x10-8
8.0x10-8
1.0x10-7
1.2x10-7
Pres
sure
[Tor
r]
Time [s]
F HF Li Na K
Plasma interaction region
29000 30000 31000 32000
0.0
3.0x10-8
6.0x10-8
9.0x10-8
1.2x10-7
1.5x10-7
1.8x10-7
2.1x10-7
2.4x10-7
2.7x10-7
Pres
sure
[Tor
r]
Time [s]
F HF Li Na K
Plasma interaction region
5min
RGA DATA – HF MEASUREMENT
The potasium is the main element from the molten salt evaporation .
Hydrogen fluoride forma-tion increase with plasma interaction time.
It is possibly come from the chemical formation of HF.
Plasma irradiation time
Plasma irradiation time
Plasma irradiation time
10min
20min
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H2 retention depends on the interaction time with H2 Plasma
1 10 100 10001E-8
1E-7
1E-6
H2 plasma
exposure time (1mTorr)
Pr H
2 [Tor
r]
Time[sec]
ref 5min 10min 20min 40min
w/o plasma
0 1000 2000 3000 4000 5000
0
1
2
3
4
5
640min
20min
10min
Out
gass
ed H
2 [cc]
Time[sec]
5min
Measured the partial pressure of out-gassed H2 from the molten salt surface as a reference without plasma interaction. The difference between the measured lines and reference have been integrated with the time to convert into the total amount of the hydrogen molecules retention.
H2 RETENTION - RESULTS
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Plasma interaction time [sec] 300 600 1200 2400
Hydrogen Dose into molten Salt [cc] 2.45 4.9 9.8 19.6
H2 retention of FLiNaK [cc] 1 1.7 3.4 6
Ratio [%] 40.8 34.7 34.7 30.6
Plasma interaction time [sec] 300 600 1200 2400Hydrogen Dose into molten Salt [cc] 4.9 9.8 19.6 39.2
H2 retention of FLiNaK [cc] 1 1.7 3.4 6Ratio [%] 20.4 17.3 17.3 15.3
Considering on High Energy Neutral Particles by the Charge Exchange in the Pre-sheath
Considering only the ion bombardment on the Molten Salt
H2 RETENTION - RESULTS Hydrogen retention mainly result from the ion flux into the
molten salts. If the charge exchange which is the high energy neutral particle
formation process in the pre-sheath is considered, the retention ratio will be decreased by factor 2.
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SUMMARY and FUTURE PLANS
Sodium and Potasium are main impurities from the molten salt. Fluorine forms the Hydrogen fluoride molecules, which is very
corrosive, by chemical reaction at the surface of molten salt or in the bulk plasma.
The composition of the molten salt changed with the interaction time and the position of molten salt.
The amount of hydrogen retention in the molten salt is about 30-40% when the charge exchange in the pre-sheath not in-cluded.
We need to understand some issues in the near future The analysis methods to evaluate the composition of the molten salt.
Physical properties, especially viscosity of molten salt, after plasma interaction.
The impurities from the molten salt, quantitatively. Influence of HF to the structure.
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1
2
3
4
1170 mm
1030 mm
ECR
Helicon
Length of Pipe [mm] Vol. [cc]1 700 1374.4 2 500 981.7 3 600 1178.1 4 400 785.4 Total volume [cc] 4319.7
Total mass of molten salt [kg] 2.1
Roughly request minimum Molten Salt over 4kg Conceptual design parameters for the flowing system
Helicon and ECR are the candidates of the plasma sources
CONCEPTUAL DESIGN OF THE FLOWING SYSTEM
3
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FUTURE PLANS – ROAD MAP
2012
2015
2018
2020 -
2010
CPC will move to the new site in 2012. The flowing system of the molten
salt will be built.
The linear device will be operated in 2015.
New molten salt, such as FLiBe, FLiNaBe, will be studied from 2018
Molten Salt exp. in a Torus device from 2020 ?